METHOD TO PREPARE VIRTUAL ASSAY USING NEAR INFRARED SPECTROSCOPY
20230274801 · 2023-08-31
Inventors
Cpc classification
G16C20/30
PHYSICS
G01N11/00
PHYSICS
International classification
G16C20/20
PHYSICS
G01N11/00
PHYSICS
Abstract
Systems and methods are disclosed for providing virtual assays of an oil sample such as crude oil based on near infrared (NIR) spectroscopy carried out on the oil sample, and the density of the oil sample. The virtual assay provides a full range of information about fractions of the oil sample including naphtha, gas oil, vacuum gas oil, vacuum residue, and other information about the properties of the oil sample. Using the system and method herein, the virtual assay data pertaining to these several fractions of the oil sample and the oil sample itself are obtained without the need to fractionate the oil sample into the several components.
Claims
1. A method for producing a virtual assay of an oil sample, wherein the oil sample is characterized by a density, selected from the group consisting of crude oil, bitumen and shale oil, and characterized by naphtha, gas oil, vacuum gas oil and vacuum residue fractions, the method comprising: entering into a computer near infrared (NIR) spectroscopy data indicative of absorbance values of the oil sample over a predetermined wavenumber range obtained by analysis of the oil sample without distillation; calculating and assigning an analytical value (AV) as a function of the NIR spectroscopy data; and calculating and assigning, as a function of the AV and the density of the oil sample, virtual assay data of the oil sample and the naphtha, gas oil, vacuum gas oil and vacuum residue fractions, said virtual assay data comprising a plurality of assigned data values.
2. The method of claim 1, wherein virtual assay data comprises: a plurality of assigned assay data values pertaining to the oil sample including one or more of aromatic content, C5-asphaltenes content, elemental compositions of sulfur and nitrogen, micro-carbon residue content, total acid number and viscosity; a plurality of assigned assay values pertaining to the vacuum residue fraction of the oil sample including one or more of elemental composition of sulfur and micro-carbon residue content; a plurality of assigned assay values pertaining to the vacuum gas oil fraction of the oil sample including elemental compositions of one or more of sulfur and nitrogen; a plurality of assigned assay values pertaining to the gas oil fraction of the oil sample including one or more of elemental compositions of sulfur and nitrogen, viscosity, and indicative properties including aniline point, cetane number, cloud point and pour point; and a plurality of assigned assay values pertaining to the naphtha fraction of the oil sample including one or more of aromatic content, elemental composition of hydrogen and sulfur, paraffin content and octane number.
3. The method of claim 1, wherein virtual assay data comprises: a plurality of assigned assay data values pertaining to the oil sample including aromatic content, C5-asphaltenes content, elemental compositions of sulfur and nitrogen, micro-carbon residue content, total acid number and viscosity; a plurality of assigned assay values pertaining to the vacuum residue fraction of the oil sample including elemental composition of sulfur and micro-carbon residue content; a plurality of assigned assay values pertaining to the vacuum gas oil fraction of the oil sample including elemental compositions of sulfur and nitrogen; a plurality of assigned assay values pertaining to the gas oil fraction of the oil sample including elemental compositions of sulfur and nitrogen, viscosity, and indicative properties including aniline point, cetane number, cloud point and pour point; and a plurality of assigned assay values pertaining to the naphtha fraction of the oil sample including aromatic content, elemental composition of hydrogen and sulfur, paraffin content and octane number.
4. The method of claim 3, wherein virtual assay data further comprises: yields of fractions from the oil sample as mass fractions of boiling point ranges, including one or more of naphtha, gas oil, vacuum gas oil and vacuum residue; composition information of hydrogen sulfide and/or mercaptans in the oil sample and/or its fractions; elemental compositions of one or more of carbon, hydrogen, nickel, and vanadium; physical properties of the oil sample and/or its fractions including one or more of API gravity and refractive index; or indicative properties of the oil sample and/or its fractions including one or more of flash point, freezing point and smoke point.
5. The method of claim 1, further comprising operating a near infrared spectrometer to obtain the NIR spectroscopy data indicative of absorbance values of the oil sample over the predetermined wavenumber range, by directly analyzing the oil sample.
6. (canceled)
7. The method of claim 1, wherein each assay value is determined by a multi-variable polynomial equation with predetermined constant coefficients developed using linear regression techniques, wherein corresponding variables are the AV and the density of the oil sample.
8. The method of claim 7, wherein each assay value is determined by
AD=K.sub.AD+X1.sub.AD*AV+X2.sub.AD*AV.sup.2+X3.sub.AD*AV.sup.3+X4.sub.AD*ρ*AV where: AD is the assigned assay value that is a value and/or property representative of an elemental composition value, a physical property or an indicative property; AV is the analytical value of the oil sample; ρ is the density of the oil sample; and K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, and X4.sub.AD are constants.
9. The method of claim 7, wherein each assay value is determined by
AD=K.sub.AD+X1.sub.AD*ρ+X2.sub.AD*ρ.sup.2+X3.sub.AD*ρ.sup.3+X4.sub.AD*AV+X5.sub.AD*AV.sup.2+X6.sub.AD*AV.sup.3+X7.sub.AD*ρ*AV where: AD is the assigned assay value that is a value and/or property representative of an elemental composition value, a physical property or an indicative property; AV is the analytical value of the oil sample; ρ is the density of the oil sample; and K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, X4.sub.AD, X5.sub.AD, X6.sub.AD and X7.sub.AD are constants.
10. The method of claim 8, wherein the analytical value is a near infrared absorbance index (NIRA).
11. The method of claim 10, wherein the NIRA is calculated from a summation of the absorbance values for the values detected by the near infrared spectrometer in the predetermined wavenumber range.
12. The method of claim 10, wherein
13. A system for producing a virtual assay of an oil sample, wherein the oil sample is characterized by a density, selected from the group consisting of crude oil, bitumen and shale oil, and characterized by naphtha, gas oil, vacuum gas oil and vacuum residue fractions, the system comprising: a near infrared (MR) spectrometer that outputs near infrared spectroscopy data; a non-volatile memory device that stores calculation modules and data, the data including the NIR spectroscopy data, wherein the NIR spectroscopy data is indicative of absorbance values of the oil sample over a predetermined wavenumber range obtained by analysis of the oil sample without distillation; a processor coupled to the non-volatile memory device; a first calculation module that is stored in the non-volatile memory device and that is executed by the processor, wherein the first calculation module calculates an analytical value (AV) as a function of the NIR spectroscopy data; and a second calculation module that is stored in the non-volatile memory device and that is executed by the processor, wherein the second calculation module calculates, as a function of the AV and the density of the oil sample, virtual assay data of the oil sample and the naphtha, gas oil, vacuum gas oil and vacuum residue fractions, said virtual assay data comprising a plurality of assigned data values.
14. The system as in claim 13, wherein virtual assay data comprises: a plurality of assigned assay data values pertaining to the oil sample including aromatic content, C5-asphaltenes content, elemental compositions of sulfur and nitrogen, micro-carbon residue content, total acid number and viscosity; a plurality of assigned assay values pertaining to the vacuum residue fraction of the oil sample including elemental composition of sulfur and micro-carbon residue content; a plurality of assigned assay values pertaining to the vacuum gas oil fraction of the oil sample including elemental compositions of sulfur and nitrogen; a plurality of assigned assay values pertaining to the gas oil fraction of the oil sample including elemental compositions of sulfur and nitrogen, viscosity, and indicative properties including aniline point, cetane number, cloud point and pour point; a plurality of assigned assay values pertaining to the naphtha fraction of the oil sample including aromatic content, elemental composition of hydrogen and sulfur, paraffin content and octane number.
15. The system as in claim 14, wherein virtual assay data further comprises: yields of fractions from the oil sample as mass fractions of boiling point ranges, including one or more of naphtha, gas oil, vacuum gas oil and vacuum residue; composition information of hydrogen sulfide and/or mercaptans in the oil sample and/or its fractions; elemental compositions of one or more of carbon, hydrogen, nickel, and vanadium; physical properties of the oil sample and/or its fractions including one or more of API gravity and refractive index; or indicative properties of the oil sample and/or its fractions including one or more of flash point, freezing point and smoke point.
16. The system of claim 13, wherein each assay value is calculated and assigned by the second calculation module with a multi-variable polynomial equation with predetermined constant coefficients developed using linear regression techniques, wherein corresponding variables are the AV and the density of the oil sample.
17. The system of claim 16, wherein each assay value is calculated and assigned by the second calculation module with a function:
AD=K.sub.AD+X1.sub.AD*AV+X2.sub.AD*AV.sup.2+X3.sub.AD*AV.sup.3+X4.sub.AD*ρ*AV where: AD is the assigned assay value that is a value and/or property representative of an elemental composition value, a physical property or an indicative property; AV is the analytical value of the oil sample; ρ is the density of the oil sample; and K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, and X4.sub.AD are constants.
18. The system claim 16, wherein each assay value is calculated and assigned by the second calculation module with the function:
AD=K.sub.AD+X1.sub.AD*ρ+X2.sub.AD*ρ.sup.2+X3.sub.AD*ρ.sup.3+X4.sub.AD*AV+X5.sub.AD*AV.sup.2+X6.sub.AD*AV.sup.3+X7.sub.AD*ρ*AV where: AD is the assigned assay value that is a value and/or property representative of an elemental composition value, a physical property or an indicative property; AV is the analytical value of the oil sample; ρ is the density of the oil sample; and K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, X4.sub.AD, X5.sub.AD, X6.sub.AD and X7.sub.AD are constants.
19. The system of claim 18, wherein the analytical value is a near infrared absorbance index (NIRA).
20. The system of claim 19, wherein the NIRA is calculated from a summation of the absorbance values for the values detected by the near infrared spectrometer in the predetermined wavenumber range.
21. The system of claim 19, wherein
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0038]
[0039]
[0040]
[0041]
DETAILED DESCRIPTION
[0042] Systems and methods are disclosed for providing virtual assays of an oil sample such as crude oil based on near infrared (NIR) spectroscopy carried out on the oil sample, and the density of the oil sample. The virtual assay provides a full range of information about fractions of the oil sample including naphtha, gas oil, vacuum gas oil, vacuum residue, and other information about the properties of the oil sample. Using the system and method herein, the virtual assay data pertaining to these several fractions of the oil sample and the oil sample itself is obtained without the need for fractionation of the oil sample into the several components.
[0043] Concerning the naphtha fraction, assigned assay values for the virtual assay include: elemental composition values included in the virtual assay comprise one or more of hydrogen content, aromatic content, paraffin content and sulfur content; and an indicative property included in the virtual assay comprises an octane number. Concerning the gas oil fraction, assigned assay values for the virtual assay include: elemental composition values included in the virtual assay comprise one or more of sulfur content and nitrogen content; physical properties included in the virtual assay comprises viscosity and pour point; and indicative properties included in the virtual assay comprise one or more of aniline point, cetane number and cloud point. Concerning the vacuum gas oil fraction, assigned assay values for the virtual assay include: elemental composition values included in the virtual assay comprise one or more of sulfur content, nitrogen content and micro carbon residue content. Concerning the vacuum residue, assigned assay values for the virtual assay include: elemental composition values included in the virtual assay comprise one or more of sulfur content and micro carbon residue content. Concerning the full range of the oil sample, assigned assay values for the virtual assay include: elemental composition values included in the virtual assay comprise one or more of asphaltene content, sulfur content, nitrogen content and total acids content (total acid number, mg KOH/100 g); and physical properties included in the virtual assay comprises viscosity and pour point.
[0044] In certain embodiments of the virtual assay provided herein, the “naphtha fraction” refers to a straight run fractions from atmospheric distillation containing hydrocarbons having a nominal boiling range of about 20-205, 20-193, 20-190, 20-180, 20-170, 32-205, 32-193, 32-190, 32-180, 32-170, 36-205, 36-193, 36-190, 36-180 or 36-170° C.; the “gas oil fraction” refers to a straight run fractions from atmospheric distillation containing hydrocarbons having a nominal boiling range of about 170-400, 170-380, 170-370, 170-360, 180-400, 180-380, 180-370, 180-360, 190-400, 190-380, 190-370, 190-360, 193-400, 193-380, 193-370 or 193-360° C.; the “vacuum gas oil fraction” refers to a straight run fractions from vacuum distillation containing hydrocarbons having a nominal boiling range of about 360-565, 360-550, 360-540, 360-530, 360-520, 360-510, 370-565, 370-550, 370-540, 370-530, 370-520, 370-510, 380-565, 380-550, 380-540, 380-530, 380-520, 380-510, 400-565, 400-550, 400-540, 400-530, 400-520 or 400-510° C.; and “vacuum residue” refers to the bottom hydrocarbons from vacuum distillation having an initial boiling point corresponding to the end point of the VGO range hydrocarbons, for example about 510, 520, 530, 540, 550 or 565° C., and having an end point based on the characteristics of the crude oil feed.
[0045] The system and method is applicable for naturally occurring hydrocarbons derived from crude oils, bitumens or shale oils, and heavy oils from refinery process units including hydrotreating, hydroprocessing, fluid catalytic cracking, coking, and visbreaking or coal liquefaction. Samples can be obtained from various sources, including an oil well, core cuttings, oil well drilling cuttings, stabilizer, extractor, or distillation tower. In certain embodiments system and method is applicable for crude oil, whereby a virtual assay is obtained using the systems and methods herein without the extensive laboratory work required for distillation and analysis of each of the individual fractions.
[0046] Referring to
[0047] At step 110, the density if the oil sample is provided (steps for obtaining this density are not shown and can be carried out as is known, in certain embodiments a 15° C./4° C. density in units of kilograms per liter using the method described in ASTM D4052); this density value can be stored in memory with other data pertaining to the oil sample, or conveyed directly to the one or more steps as part of the functions thereof. In step 115, if necessary, the oil sample is prepared for a particular analytic characterization technique (shown in dashed lines as optional). In step 120, analytic characterization of the oil sample, or the oil sample prepared as in step 115, without fractionation, is carried out. As a result, analytic characterization data 125 is obtained.
[0048] In step 130, the analytic characterization data 125 is used to calculate one or more analytical values 135, which are one common analytical value or a common set of analytical values used in subsequent steps to calculate a plurality of different elemental composition values/physical properties/indicative properties that make up the virtual assay. In the embodiments herein the one common analytical value or common set of analytical values includes one or more index values, also referred to as a NIRA, obtained from NIR spectra data including a range of absorbance values or peaks over a range of wavenumbers.
[0049] Steps 140, 150, 160, 170 and 180 are used to calculate and assign a plurality of different elemental composition values/physical properties/indicative properties that make up the virtual assay 195, for each of a total oil sample, a naphtha fraction, a gas oil fraction, a vacuum gas oil fraction and a vacuum residue fraction, respectively. Each of the steps produces corresponding assigned assay values for the virtual assay 195, include including assigned assay values 145 pertaining to the total oil sample, assigned assay values 155 pertaining to a naphtha fraction, assigned assay values 165 pertaining to a gas oil fraction, assigned assay values 175 pertaining to a vacuum gas oil fraction and assigned assay values 185 pertaining to a vacuum residue fraction.
[0050] In certain embodiments, the steps are carried out in any predetermined sequence, or in no particular sequence, depending on the procedures in the calculation modules. In certain embodiments, the steps are carried out in parallel. The process herein uses a common analytical value, in conjunction with the set of constants and the density of the oil sample, for each of the assigned assay values (elemental composition values/physical properties/indicative properties) in the given virtual oil sample assay 195 produced at step 190. For instance, each of the steps 140, 150, 160, 170 and 180 are carried in any sequence and/or in parallel out as show using the equations herein for various analytical values or sets of analytical values.
[0051] The assigned assay values from each of the fractions and the total oil sample are compiled and presented as a virtual assay 195, which can be, for instance, printed or rendered on a display visible to, or otherwise communicated to, a user to understand the composition and properties of the crude. With the virtual assay 195, users such as customers, producers, refiners, and marketers can benchmark the oil quality. The virtual assay 195 can be used to guide decisions related to an appropriate refinery or refining unit, for processing the oil from which the oil sample is obtained, and/or for processing one or more of the fractions thereof. In addition the assigned assay values including the indicative properties are used to determine the engine/fuel performance or usability or flow characteristic or composition. This can be accomplished using the method and system herein without performing the customary extensive and time-consuming crude oil assays.
[0052] The assigned assay values for the virtual assay herein are calculated as a function of one or more analytical values, and the density of the oil sample, as denoted at (1).
AD=f(ρ,AV) (1)
[0053] where: [0054] AD is the assigned assay value (for example a value and/or property representative of an elemental composition value, a physical property or an indicative property); [0055] AV is an analytical value of the oil sample, wherein AV can be a single analytical value, or wherein AV can be AV(1) . . . AV(n) as plural analytical values of the oil sample, wherein n is an integer of 2 or more, in certain embodiments 2, 3 or 4; and [0056] ρ is the density of the oil sample, in certain embodiments a 15° C./4° C. density in units of kilograms per liter using the method described in ASTM D4052.
[0057] According to an embodiment of the system and method described herein, an analytical value AV is a singe value, an index value derived from a summation of absorbance values over a range of wavelengths obtained using NIR spectroscopy carried out on the oil sample, represented herein as a NIR absorbance index. Advantageously, the method and system herein deploy analytical characterization by NIR spectroscopy to carry out analysis of the oil sample without fractionating, obtain an analytical value or set of analytical values based on the NIR spectroscopy analysis of the oil sample, and use the analytical value or set of analytical values, and the density of the oil sample, to obtain a plurality of assigned assay values (for example a value and/or property representative of an elemental composition value, a physical property or an indicative property) to produce a virtual assay of the oil sample.
[0058] In one embodiment, an assigned assay value is calculated used a third degree multi variable polynomial equation including the analytical value, the density of the oil sample, and a plurality of constants, for example predetermined by linear regression, as denoted in equation (2a).
AD=K.sub.AD+X1.sub.AD*AV+X2.sub.AD*AV.sup.2+X3.sub.AD*AV.sup.3+X4.sub.AD*ρ*AV (2a)
[0059] where: [0060] AD is the assigned assay value (for example a value and/or property representative of an elemental composition value, a physical property or an indicative property); [0061] AV is an analytical value of the oil sample; [0062] ρ is the density of the oil sample, in certain embodiments a 15° C./4° C. density in units of kilograms per liter using the method described in ASTM D4052; and [0063] K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, and X4.sub.AD are constants, for instance, developed using linear regression techniques (note that in certain embodiments and for certain assigned assay values, one or more of K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD and X4.sub.AD is/are not used, or is/are zero).
[0064] In another embodiment, an assigned assay value is calculated used a third degree multi variable polynomial equation including the analytical value, the density of the oil sample, and a plurality of constants, for example predetermined by linear regression, as denoted in equation (2b).
AD=K.sub.AD+X1.sub.AD*ρ+X2.sub.AD*ρ.sup.2+X3.sub.AD*ρ.sup.3+X4.sub.AD*AV+X5.sub.AD*AV.sup.2+X6.sub.AD*AV.sup.3+X7.sub.AD*ρ*AV (2b)
[0065] where: [0066] AD is the assigned assay value (for example a value and/or property representative of an elemental composition value, a physical property or an indicative property); [0067] AV is an analytical value of the oil sample; [0068] ρ is the density of the oil sample, in certain embodiments a 15° C./4° C. density in units of kilograms per liter using the method described in ASTM D4052; and [0069] K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, X4.sub.AD, X5.sub.AD, X6.sub.AD and X7.sub.AD are constants, for instance, developed using linear regression techniques (note that in certain embodiments and for certain assigned assay values, one or more of K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, X4.sub.AD, X5.sub.AD, X6.sub.AD and X7.sub.AD is/are not used, or is/are zero).
[0070] Assigned assay values that can be determined and included for display or presentation to the user in the virtual assay produced using the systems and methods herein include one or more of: [0071] elemental composition of the oil sample and its fractions including the sulfur and nitrogen compositions; [0072] TAN (total acid number) of the oil sample; [0073] composition of certain desirable and undesirable compounds or types of compounds present in the oil sample and/or its fractions, including one or more of micro carbon residue, C5-asphaltenes (the yield of asphaltenes using separation based on C5 paraffins as deasphalting solvent), paraffins, aromatics, and naphthenes; [0074] physical properties of the oil sample and/or its fractions including viscosity such as kinematic viscosity; [0075] indicative properties of the oil sample and/or its fractions, including one or more of cloud point, pour point, research octane number, cetane number and aniline point.
In certain embodiments, the assigned assay values can include yields of fractions from the oil sample, for example as mass fractions of boiling point ranges, including one or more of naphtha, gas oil, vacuum gas oil and vacuum residue. In certain embodiments, the assigned assay values can include composition information of hydrogen sulfide and/or mercaptans in the oil sample and/or its fractions. In certain embodiments, the assigned assay values can include elemental compositions of one or more of carbon, hydrogen, nickel, and vanadium. In certain embodiments, the assigned assay values can include physical properties of the oil sample and/or its fractions including one or more of API gravity and refractive index. In certain embodiments, the assigned assay values can include indicative properties of the oil sample and/or its fractions including one or more of flash point, freezing point and smoke point.
[0076] In certain embodiments, a method for producing a virtual assay of an uncharacterized oil sample is provided. The uncharacterized oil sample is characterized by a density, selected from the group consisting of crude oil, bitumen and shale oil, and characterized by naphtha, gas oil, vacuum gas oil and vacuum residue fractions. The virtual assay comprises a plurality of assigned data values. The uncharacterized oil sample is obtained, for instance the sample being between one to two milliliters in volume and not subject to any fractionation. A plurality of known data values (corresponding to the assigned data values used in the virtual assay) for known oil samples with known densities (which known oil samples exclude the uncharacterized oil sample) are obtained. This data is obtained from empirical data of a plurality of existing crude oil assays and/or analyses using conventional techniques including distillation and industry-established testing methods. One or more selected analytical techniques are carried out on the each of the known oil samples, and one or more analytical values are calculated for each of the known oil samples. The one or more selected analytical techniques are carried out on the uncharacterized oil sample, and one or more analytical values are calculated for the uncharacterized oil sample. Constants of a polynomial equation are obtained, and the polynomial equation is used to determine a plurality of assigned data values that make up the virtual assay of the uncharacterized oil sample. The polynomial equation is a function of density and the one or more analytical values of the uncharacterized oil sample. The constants of the polynomial equation are determined using a fitting method to fit the plurality of known data values of the plurality of known oil samples to the plurality of values of the density of the plurality of known oil samples and the plurality of the one or more analytical values for the plurality of known oil samples.
[0077] Rather than relying on conventional techniques including distillation and laborious, costly and time-consuming analytical methods to measure/identify data regarding the crude oil and/or its fractions including elemental composition, physical properties and indicative properties, as little as 1 gram of oil can be analyzed. From the analysis of a relatively small quantity of the oil sample, the assigned assay values are determined by direct calculation, without requiring distillation/fractionization.
[0078] NIR spectroscopy is the analytic characterization technique that is employed on a relatively small quality of an oil sample, such as crude oil. The analytic characterization system and corresponding technique is carried out using the full range of the oil sample, without fractionating. An analytical value, comprising or consisting of the NIR absorbance index of the oil sample from said analytic characterization technique, is used to calculate and assign physical and indicative properties that are the requisite data for the virtual oil sample assay. The method and system provide insight into the properties of oil sample, the naphtha fraction, the gas oil fraction, the vacuum gas oil fraction, and the vacuum residue fraction, without fractionation/distillation (conventional crude oil assays). The virtual oil sample assay will help producers, refiners, and marketers benchmark the oil quality and, as a result, evaluate (qualitatively and economically) the oils without going thru costly and time consuming crude oil assays. Whereas a conventional crude oil assay method could take up to two months, the method and system herein can provide a virtual assay in less than one day and in certain embodiments less than 1-2 hours. In addition, the method and system herein carried out at 1% or less of the cost of a traditional assay requiring distillation/fractionization follows by individual testing for each type of property and for each fraction.
[0079] The systems and methods herein are implemented using an index derived from NIR spectroscopy data as an analytical value in equations (1), and (2a) or (2b), above. Embodiments of such methods are described in the context of assigning an indicative property to a fraction of an oil sample in commonly owned U.S. Ser. No. 10/677,718B2, which is incorporated by reference herein in its entirety. In the systems and methods herein, and with reference to
[0080] The oil sample is optionally prepared, step 115, by dissolving the oil sample in a suitable solvent for NIR spectroscopy. For example, in certain embodiments, a solution is prepared by dissolving the oil sample in a suitable solvent such as a paraffinic solvent for which NIR spectroscopy data is known, and thus can be subtracted from the NIR spectrum to yield accurate NIR spectroscopy data pertaining to the oil sample. In certain embodiments, the oil sample can be directly analyzed in the absence of a solvent, and step 115 is avoided, and accordingly step 115 is shown in dashed lines in
[0081] The solution or oil sample is analyzed, step 120, and NIR spectroscopy data is obtained. Step 120 is carried out and the analytic characterization data, the NIR spectroscopy data, is entered into the computer system 400 described herein with respect to
[0082] An analytical value is obtained, step 130, as a function of absorbance of the oil sample over a range of wavelengths. In certain embodiments the analytical value obtained from the NIR spectroscopy data includes an index of the oil sample described herein, for instance obtained as a function of a summation of absorbance values over a range of wavenumbers, the NIR absorbance index. Step 130 is carried out, for example, by execution by the processor 420 of one or more modules stored in the program storage memory 470, and the analytical values 135, the index, is stored in the program storage memory 470 or the data storage memory 480, for use in the modules determining the assigned data values. In certain embodiments, the density of the oil sample, provided at step 110, is stored in the program storage memory 470 or the data storage memory 480, for use in the modules determining the assigned data values; this can be carried out by a raw data receiving module stored in the program storage memory 470.
[0083] The assigned data values including virtual assay data 145 pertaining to the total oil sample, virtual assay data 155 pertaining to a naphtha fraction, virtual assay data 165 pertaining to a gas oil fraction, virtual assay data 175 pertaining to a vacuum gas oil fraction, virtual assay data 185 pertaining to a vacuum residue fraction, are obtained according to the functions described herein, for example, in the corresponding steps 140, 150, 160, 170 and 180. The constants used for determining the assigned data values, are provided at step 105 and are stored in the program storage memory 470 or the data storage memory 480, for use in the modules determining the assigned data values. The steps for obtaining the assigned data values are carried out, for example, by execution by the processor 420 of one or more modules stored in the program storage memory 470, and the several assigned data values are calculated and stored in the data storage memory 480, presented on the display 410 and/or presented to the user by some other output device such as a printer.
[0084] The NIR spectroscopy data is obtained using suitable NIR spectroscopy apparatus as is known. Infrared energy is the electromagnetic energy of molecular vibration. The energy band is defined for convenience as the near infrared (0.78-2.50 microns), the infrared (or mid-infrared) 2.50-40.0 microns, and the far infrared (40.0-1000 microns). However, even though official standards, textbooks, and the scientific literature generally state that the NIR spectral region extends from 780-2500 nanometers (12821-4000 cm-1), a simple set of liquid phase hydrocarbon spectra demonstrates that the vibrational information characterized by the harmonic vibrations of the C—H stretch fundamental and their corresponding combination bands occurs from approximately 690-3000 nm. The predominant near-infrared spectral features include: the methyl C—H stretching vibrations, methylene C—H stretching vibrations, aromatic C—H stretching vibrations, and O—H stretching vibrations. Minor but still important spectral features include: methoxy C—H stretching, carbonyl associated C—H stretching; N—H from primary amides, secondary amides (both alkyl, and aryl group associations), N—H from primary, secondary, and tertiary amines, and N—H from amine salts.
[0085] Qualitative and quantitative NIR spectroscopic methods typically require the application of multivariate calibration algorithms and statistical methods (i.e. chemometrics) to model NIR spectral response to chemical or physical properties of the samples used for calibration. The NIR method relies on the spectra-structure correlations existing between a measured spectral response caused by the harmonics of the fundamental vibrations occurring at infrared frequencies. These harmonic vibrations occur at unique frequencies depending upon the quantity of absorber (analyte), type of absorbing molecules present within the sample, and the sample thickness. Quantitative methods are possible where changes in the response of the near infrared spectrometer are proportional to changes in the concentration of chemical components, or in the physical characteristics (scattering/absorptive properties) of samples undergoing analysis.
[0086] Near infrared spectroscopy is used where multicomponent molecular vibrational analysis is required in the presence of interfering substances. The near infrared spectra consist of overtones and combination bands of the fundamental molecular absorptions found in the mid infrared region. Near infrared spectra consist of generally overlapping vibrational bands that may appear non-specific and poorly resolved. The use of chemometric mathematical data processing and multiple harmonics can be used to calibrate for qualitative of quantitative analysis despite these apparent spectroscopic limitations. Traditional near infrared spectroscopy has been most often used for analysis of lignin polymers (2270 nm), paraffins and long alkane chain polymers (2310 nm), glucose based polymers such as cellulose (2336 nm), amino acid polymers as proteins (2180 nm), carbohydrates (2100 nm), and moisture (1440 and 1940 nm). When analyzing synthetic and natural materials NIR spectroscopy has shown unprecedented industrial success in multiple applications. The basic uses of near infrared spectroscopy have been for process control, quality assessment, identification of raw materials and process byproducts, and chemical quantitative analysis of complex mixtures.
[0087] A near infrared spectrum consists in the convolution of the measuring instrument function with the unique optical characteristics of the sample being measured (i.e. the sample is an active optical element of the spectrometer). The reference values are those chemical or physical parameters to be predicted using the NIR spectroscopic measurements. A spectrum may, or may not, contain information related to the sample chemistry measured using any specific reference method. Spectra-structure correlation provides a basis for the establishment of a known cause and effect relationship between instrument response and reference (analyte) data, in order to provide a more scientific basis for multivariate-based near infrared spectroscopy. When performing multivariate calibrations, analytically valid calibration models require a relationship between X (the instrument response data or spectrum) and Y (the reference data). The use of probability alone tells us only if X and Y “appear” to be related. If no cause-effect relationship exists between spectra-structure correlation and reference values the model will have no true predictive importance. Thus, knowledge of cause and effect creates a basis for scientific decision-making.
[0088] Factors affecting the integrity of the teaching samples used to calibrate spectrophotometers for individual NIR applications include the variations in sample chemistry, the physical condition of samples, and the measurement conditions. Teaching sets must represent several sample “spaces” to include: compositional space, instrument space, and measurement condition (sample handling and presentation) space. Interpretive spectroscopy is a key intellectual process in approaching NIR measurements if one is to achieve an analytical understanding of these measurements.
[0089] Near-infrared spectroscopy has been employed for the characterization of products derived from petroleum, such as gasoline and diesel fuel, with considerable success. The intrinsic capacity of the NIR spectrum to obtain information on the different types of C—H bonds as well as other chemical bonds of interest (such as S—H and N—H) has been proved to be valuable in the prediction of quality parameters such as octane number, ethanol content, MTBE (methyl tert-butyl ether) content, distillation points, Reid vapor pressure and aromatic and saturated contents in gasoline. The information present in the NIR spectrum obtained from analysis of individual fractions can be successfully applied to the prediction of quality parameters for diesel fuel such as cetane number, distillation points, density, viscosity and sulfur content.
[0090] The determination of the assigned data is carried out using variables comprising or consisting of the NIRA of the oil sample and the density of the oil sample.
AD=f(ρ,NIRA)) (3)
[0091] where: [0092] AD is the assigned data value (for example a value and/or property representative of an elemental composition value, a physical property or an indicative property); [0093] NIRA=index derived from a summation of absorbances over a predetermined range of wavenumbers, as determined by NIR spectroscopy of the oil sample; and [0094] ρ is the density of the oil sample, in certain embodiments a 15° C./4° C. density in units of kilograms per liter using the method described in ASTM D4052.
[0095] For example, this relationship can be expressed as follows:
AD=K.sub.AD+X1.sub.AD*ρ+X2.sub.AD*ρ.sup.2+X3.sub.AD*ρ.sup.3+X4.sub.AD*NIRA+X5.sub.AD*NIRA.sup.2+X6.sub.AD*NIRA.sup.3+X7.sub.AD*ρ*NIRA (4)
[0096] where AD, NIRA and ρ are as in equation (3), and where: [0097] K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, X4.sub.AD, X5.sub.AD, X6.sub.AD and X7.sub.AD are constants, for instance, developed using linear regression techniques, for each AD to be determined (note that in certain embodiments and for certain assigned assay values, one or more of K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, X4.sub.AD, X5.sub.AD, X6.sub.AD and X7.sub.AD is/are not used, or is/are zero).
[0098] Using the equation (4), one or more assigned data values AD are determined using the density of the oil sample and the NIRA of the oil sample, as determined by NIR spectroscopy of the oil sample.
[0099] Table 3 lists assigned data for a virtual assay of an oil sample under investigation, with descriptions, abbreviations and units, for each assigned data property for the naphtha fraction, the gas oil fraction, the vacuum gas oil fraction, the vacuum residue fraction and the overall oil sample. Table 3 further provides exemplary constants, for instance, developed using linear regression techniques, for plural assigned data values to be determined based on the density of the oil sample and the NIRA of the oil sample. These constants are used in the example below with the calculated values provided in Table 5 compared to the actual values as determined by a conventional crude oil assay.
[0100] The constants, for example as in Table 3, are stored as in step 105 in the process flow diagram of
[0101] In certain embodiments, the assigned data values including virtual assay data 145 pertaining to the total oil sample, virtual assay data 155 pertaining to a naphtha fraction, virtual assay data 165 pertaining to a gas oil fraction, virtual assay data 175 pertaining to a vacuum gas oil fraction and virtual assay data 185 pertaining to a vacuum residue fraction. This data is obtained according to the function (3) described above (for example expressed as in equation (4) described above, for example, with the corresponding modules/steps 140, 150, 160, 170 and 180.
[0102] In certain embodiments, the analytical value obtained as in step 130 is a NIRA of the oil sample determined as follows:
[0103] where: [0104] i is a range of wavenumbers, for example, in a range of from 4000-12821 cm.sup.−1; and [0105] Absorbance=absorbance value of the oil sample for values detected at wavenumbers over the range i, in absorbance units.
Example
[0106] Crude oil samples, including a crude oil sample as the oil sample under investigation, were analyzed by NIR spectroscopy according to the methods described herein.
[0107] At step 330, an analytical value, the near infrared spectroscopy index (NIRA), is calculated by summing the absorbances of the detected values or peaks stored in step 325 and then dividing by 10,000, as in Equation 5 herein, with the value in the example using the data in Table 4 calculated as 0.7576.
[0108] The NIRA, stored at step 335, is applied to step 390. At step 390, Equation (4) and the constants from Table 3 are applied for each of the listed ADs, using the variable NIRA stored at step 335, the constants stored at step 305, and the density of the oil sample stored at step 310, as shown below. Each of the determined ADs can be added to a virtual assay 395 of the oil sample. For example, this can be carried out as one step, or as plural steps, for instance, similar to steps 140, 150, 160, 170 and 180 described herein in conjunction with
[0109] Equation (4) is applied to each of the ADs that make up the virtual assay including those identified in Table 3, using the corresponding units. In addition, the constants denoted in Table 3 are used as the constants K.sub.AD, X1.sub.AD, X2.sub.AD, X3.sub.AD, X4.sub.AD, X5.sub.AD, X6.sub.AD and X7.sub.AD) in equation (4); the NIRA based on the data in Table 4, calculated as 0.7576 is using equation (5) above, is used in equation (4); and the density ρ used in equation (4) for the of the oil sample under investigation is the 15° C./4° C. density in units of kilograms per liter using the method described in ASTM D4052, which is 0.8828 Kg/L. The calculated AD values are provided for the oil sample under investigation in Table 5, compared to the actual values obtained using a conventional crude oil assay.
[0110]
[0111] Program storage memory 470 and data storage memory 480 can each comprise volatile (RAM) and non-volatile (ROM) memory units and can also comprise hard disk and backup storage capacity, and both program storage memory 470 and data storage memory 480 can be embodied in a single memory device or separated in plural memory devices. Program storage memory 470 stores software program modules and associated data and stores one or more of: a raw data receiving module 471, having one or more software programs adapted to receive the analytic characterization data 125, for instance obtained at step 120 in the process flow diagram of
[0112] It is to be appreciated that the computer system 400 can be any computer such as a personal computer, minicomputer, workstation, mainframe, a dedicated controller such as a programmable logic controller, or a combination thereof. While the computer system 400 is shown, for illustration purposes, as a single computer unit, the system can comprise a group of computers which can be scaled depending on the processing load and database size.
[0113] Computer system 400 generally supports an operating system, for example stored in program storage memory 470 and executed by the processor 420 from volatile memory. According to an embodiment of the invention, the operating system contains instructions for interfacing computer system 400 to the Internet and/or to private networks.
[0114] Note that steps 110 and 120 can be carried out separate from or within the computer system 400. For example, step 110 can be carried out and the data entered into the computer system 400, for example via data storage memory 480, or as a single value incorporated in the program storage memory 470 for one or more of the modules. Step 120 can be carried out and the analytic characterization data entered into the computer system 400, for example via data storage memory 480, represented as the analytic characterization data 125.
[0115] In alternate embodiments, the present invention can be implemented as a computer program product for use with a computerized computing system. Those skilled in the art will readily appreciate that programs defining the functions of the present invention can be written in any appropriate programming language and delivered to a computer in any form, including but not limited to: (a) information permanently stored on non-writeable storage media (e.g., read-only memory devices such as ROMs or CD-ROM disks); (b) information alterably stored on writeable storage media (e.g., floppy disks and hard drives); and/or (c) information conveyed to a computer through communication media, such as a local area network, a telephone network, or a public network such as the Internet. When carrying computer readable instructions that implement the present invention methods, such computer readable media represent alternate embodiments of the present invention.
[0116] As generally illustrated herein, the system embodiments can incorporate a variety of computer readable media that comprise a computer usable medium having computer readable code means embodied therein. One skilled in the art will recognize that the software associated with the various processes described can be embodied in a wide variety of computer accessible media from which the software is loaded and activated. Pursuant to In re Beauregard, 35 U.S.P.Q.2d 1383 (U.S. Pat. No. 5,710,578), the present invention contemplates and includes this type of computer readable media within the scope of the invention. In certain embodiments, pursuant to In re Nuuten, 500 F.3d 1346 (Fed. Cir. 2007) (U.S. patent application Ser. No. 09/211,928), the scope of the present claims is limited to computer readable media, wherein the media is both tangible and non-transitory.
[0117] It is to be understood that like numerals in the drawings represent like elements through the several figures, and that not all components and/or steps described and illustrated with reference to the figures are required for all embodiments or arrangements. Further, the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the singular forms “a”, “an” and “the” are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms “including,” “comprising,” or “having,” “containing,” “involving,” and variations thereof herein, when used in this specification, specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof.
[0118] It should be noted that use of ordinal terms such as “first,” “second,” “third,” etc., in the claims to modify a claim element does not by itself connote any priority, precedence, or order of one claim element over another or the temporal order in which acts of a method are performed, but are used merely as labels to distinguish one claim element having a certain name from another element having a same name (but for use of the ordinal term) to distinguish the claim elements.
[0119] Notably, the figures and examples above are not meant to limit the scope of the present disclosure to a single implementation, as other implementations are possible by way of interchange of some or all the described or illustrated elements. Moreover, where certain elements of the present disclosure can be partially or fully implemented using known components, only those portions of such known components that are necessary for an understanding of the present disclosure are described, and detailed descriptions of other portions of such known components are omitted so as not to obscure the disclosure. In the present specification, an implementation showing a singular component should not necessarily be limited to other implementations including a plurality of the same component, and vice-versa, unless explicitly stated otherwise herein. Moreover, applicants do not intend for any term in the specification or claims to be ascribed an uncommon or special meaning unless explicitly set forth as such. Further, the present disclosure encompasses present and future known equivalents to the known components referred to herein by way of illustration.
[0120] The foregoing description of the specific implementations will so fully reveal the general nature of the disclosure that others can, by applying knowledge within the skill of the relevant art(s), readily modify and/or adapt for various applications such specific implementations, without undue experimentation, without departing from the general concept of the present disclosure. Such adaptations and modifications are therefore intended to be within the meaning and range of equivalents of the disclosed implementations, based on the teaching and guidance presented herein. It is to be understood that the phraseology or terminology herein is for the purpose of description and not of limitation, such that the terminology or phraseology of the present specification is to be interpreted by the skilled artisan in light of the teachings and guidance presented herein, in combination with the knowledge of one skilled in the relevant art(s). It is to be understood that dimensions discussed or shown are drawings are shown accordingly to one example and other dimensions can be used without departing from the disclosure.
[0121] The subject matter described above is provided by way of illustration only and should not be construed as limiting. Various modifications and changes can be made to the subject matter described herein without following the example embodiments and applications illustrated and described, and without departing from the true spirit and scope of the invention encompassed by the present disclosure, which is defined by the set of recitations in the following claims and by structures and functions or steps which are equivalent to these recitations.
TABLE-US-00001 TABLE 1 Fraction Boiling Point, ° C. Methane −161.5 Ethane −88.6 Propane −42.1 Butanes −6.0 Light Naphtha 36-90 Mid Naphtha 90-160 Heavy Naphtha 160-205 Light gas Oil 205-260 Mid Gas Oil 260-315 Heavy gas Oil 315-370 Light Vacuum Gas Oil 370-430 Mid Vacuum Gas Oil 430-480 Heavy vacuum gas oil 480-565 Vacuum Residue 565+
TABLE-US-00002 TABLE 2 Property Property Unit Type Fraction Yield W % or V % Yield All API Gravity ° Physical All Kinematic Viscosity @ 38° C. cSt Physical Fraction boiling >250° C. Refractive Index @ 20° C. Unitless Physical Fraction boiling <400° C. Sulfur W % or ppmw Composition All Mercaptan Sulfur W % Composition Fraction boiling <250° C. Nickel ppmw Composition Fraction boiling >400° C. Vanadium ppmw Composition Fraction boiling >400° C. Nitrogen ppmw Composition All Flash Point ° C. Indicative All Cloud Point ° C. Indicative Fraction boiling >250° C. Pour Point ° C. Indicative Fraction boiling >250° C. Freezing Point ° C. Indicative Fraction boiling >250° C. Micro Carbon Residue W % Indicative Fraction boiling >300° C. Smoke Point mm Indicative Fraction boiling between 150-250° C. Octane Number Unitless Indicative Fraction boiling <250° C. Cetane Index Unitless Indicative Fraction boiling between 150-400° C. Aniline Point ° C. Indicative Fraction boiling <520° C.
TABLE-US-00003 TABLE 3 Fraction property Units K.sub.AD X1.sub.AD Naphtha Aromatics (Aro) W % 2.889559E+05 −9.928515E+05 Hydrogen (H) W % 2.331552E+04 −7.620349E+04 Paraffins (P) W % 1.252377E+06 −4.150454E+06 Sulfur (S) ppmw 4.334627E+04 .sup. 0000000E+00 Octane Number (ON) Unitless 4.074000E+05 −1.491697E+06 Gas Oil (GO) Aniline Point (AP) ° C. 7.607959E+05 −2.548841E+06 Cetane Number (CN) Unitless −1.818447E+05 5.763604E+05 Cloud Point (CP) ° C. −5.678452E+05 1.890385E+06 Nitrogen (N) ppmw −5.394770E+06 1.816221E+07 Sulfur (S) ppmw 7.861243E+08 −2.643680E+09 Kinematic Viscosity @40° C. cSt −1.323801E+05 4.429571E+05 Pour Point (PP) ° C. −1.373742E+06 4.551765E+06 Vacuum Gas Oil (VGO) Nitrogen (N) ppmw −2.323643E+03 0.000000E+00 Sulfur (S) ppmw −5.352648E+05 .sup. 0000000E+00 Vacuum Residue (VR) Micro Carbon Residue (MCR) W % −7.329338E+02 .sup. 0000000E+00 Sulfur (S) ppmw −9.651401E+05 .sup. 0000000E+00 Oil Sample C5-Asphaltenes (C5A) W % 1.139256E+05 −3.792392E+05 Micro Carbon Resid (MCR) W % 4.361322E+05 −1.455337E+06 Pour Point (PP) ° C. −5.062786E+06 1.689716E+07 Kinematic Viscosity @100° C. cSt 9.205567E+04 −2.771455E+05 Kinematic Viscosity @70° C. cSt 1.356083E+05 −3.600074E+05 Nitrogen (N) ppmw −5.555130E+07 1.881378E+08 Sulfur (S) ppmw 2.599763E+09 −8.728177E+09 Total Acid Number (TAN) mg KOH/100 g 4.934116E+04 −1.632319E+05 Aromatics (Aro) W % −2.440365E+05 8.115477E+05 Fraction property Units X2.sub.AD X3.sub.AD Naphtha Aromatics (Aro) W % 1.136690E+06 −4.335802E+05 Hydrogen (H) W % 8.208015E+04 −2.907995E+04 Paraffins (P) W % 4.550006E+06 −1.649119E+06 Sulfur (S) ppmw 0000000E+00 −4.734173E+04 Octane Number (ON) Unitless 1.823932E+06 −7.440324E+05 Gas Oil (GO) Aniline Point (AP) ° C. 2.831541E+06 −1.042819E+06 Cetane Number (CN) Unitless −5.932687E+05 1.968152E+05 Cloud Point (CP) ° C. −2.082457E+06 7.587736E+05 Nitrogen (N) ppmw −2.028858E+07 7.520367E+06 Sulfur (S) ppmw 2.949572E+09 −1.091767E+09 Kinematic Viscosity @40° C. cSt −4.911677E+05 1.804455E+05 Pour Point (PP) ° C. −4.984097E+06 1.802114E+06 Vacuum Gas Oil (VGO) Nitrogen (N) ppmw 0000000E+00 5.610392E+03 Sulfur (S) ppmw 0000000E+00 5.964621E+05 Vacuum Residue (VR) Micro Carbon Resid (MCR) W % 0000000E+00 8.452064E+02 Sulfur (S) ppmw 0000000E+00 1.001293E+06 Oil Sample C5-Asphaltenes (C5A) W % 4.177334E+05 −1.521804E+05 Micro Carbon Resid (MCR) W % 1.608194E+06 −5.882747E+05 Pour Point (PP) ° C. −1.867403E+07 6.831308E+06 Kinematic Viscosity @100° C. cSt 2.656226E+05 −7.915137E+04 Kinematic Viscosity @70° C. cSt 2.733291E+05 −4.494708E+04 Nitrogen (N) ppmw −2.118078E+08 7.927329E+07 Sulfur (S) ppmw 9.717825E+09 −3.587864E+09 Total Acid Number (TAN) mg KOH/100 g 1.784101E+05 −6.436734E+04 Aromatics (Aro) W % −8.919722E+05 3.239481E+05 Fraction property Units X4.sub.AD X5.sub.AD Naphtha Aromatics (Aro) W % 1.020605E+02 1.693643E+02 Hydrogen (H) W % 8.802306E+02 −1.819178E+02 Paraffins (P) W % 3.144823E+04 −5.836493E+03 Sulfur (S) ppmw −2.457974E+05 1.425574E+05 Octane Number (ON) Unitless −1.070550E+04 1.164833E+03 Gas Oil (GO) Aniline Point (AP) ° C. 1.483250E+04 −2.461449E+03 Cetane Number (CN) Unitless −1.487490E+04 1.230495E+03 Cloud Point (CP) ° C. −1.515298E+04 2.411259E+03 Nitrogen (N) ppmw −9.311482E+04 2.070216E+04 Sulfur (S) ppmw 1.313558E+07 −2.553643E+06 Kinematic Viscosity @40° C. cSt −2.858000E+03 4.628403E+02 Pour Point (PP) ° C. −4.393457E+04 5.414914E+03 Vacuum Gas Oil (VGO) Nitrogen (N) ppmw 1.502207E+04 −5.494825E+03 Sulfur (S) ppmw 2.229374E+06 −1.261744E+06 Vacuum Residue (VR) Micro Carbon Resid (MCR) W % 3.904306E+03 −2.181206E+03 Sulfur (S) ppmw 3.582861E+06 −2.746150E+06 Oil Sample C5-Asphaltenes (C5A) W % 3.147339E+03 −4.075741E+02 Micro Carbon Resid (MCR) W % 1.061290E+04 −1.410274E+03 Pour Point (PP) ° C. −1.246186E+05 1.760504E+04 Kinematic Viscosity @100° C. cSt 8.082502E+03 −1.349854E+03 Kinematic Viscosity @70° C. cSt 2.065382E+04 −3.120317E+03 Nitrogen (N) ppmw −4.832816E+05 1.155778E+05 Sulfur (S) ppmw 4.808723E+07 −8.905676E+06 Total Acid Number (TAN) mg KOH/100 g 1.606695E+03 −1.827149E+02 Aromatics (Aro) W % −7.944139E+03 1.931890E+03 Fraction property Units X6.sub.AD X7.sub.AD Naphtha Aromatics (Aro) W % −1.039042E+02 −2.180079E+02 Hydrogen (H) W % 1.028300E+02 −8.920456E+02 Paraffins (P) W % 3.251461E+03 −3.223787E+04 Sulfur (S) ppmw −8.316546E+04 1.953588E+05 Octane Number (ON) Unitless −6.138688E+02 1.146516E+04 Gas Oil (GO) Aniline Point (AP) ° C. 1.412794E+03 −1.542474E+04 Cetane Number (CN) Unitless −9.168530E+02 1.645014E+04 Cloud Point (CP) ° C. −1.430542E+03 1.587967E+04 Nitrogen (N) ppmw −1.200410E+04 9.386937E+04 Sulfur (S) ppmw 1.398321E+06 −1.336379E+07 Kinematic Viscosity @40° C. cSt −2.703467E+02 2.984608E+03 Pour Point (PP) ° C. −3.397223E+03 4.713416E+04 Vacuum Gas Oil (VGO) Nitrogen (N) ppmw 4.252311E+03 −1.644003E+04 Sulfur (S) ppmw 6.325409E+05 −1.623982E+06 Vacuum Residue (VR) Micro Carbon Resid (MCR) W % 1.197475E+03 −3.084342E+03 Sulfur (S) ppmw 1.350484E+06 −2.088010E+06 Oil Sample C5-Asphaltenes (C5A) W % 2.515484E+02 −3.358932E+03 Micro Carbon Resid (MCR) W % 8.482194E+02 −1.128212E+04 Pour Point (PP) ° C. −1.054473E+04 1.319741E+05 Kinematic Viscosity @100° C. cSt 8.017571E+02 −8.418259E+03 Kinematic Viscosity @70° C. cSt 1.866013E+03 −2.172755E+04 Nitrogen (N) ppmw −6.146279E+04 4.787340E+05 Sulfur (S) ppmw 5.003546E+06 −4.934374E+07 Total Acid Number (TAN) mg KOH/100 g 1.163813E+02 −1.734030E+03 Aromatics (Aro) W % −1.138734E+03 7.922455E+03
TABLE-US-00004 Wave- Wave- Wave- Wave- Wave- number, number, number, number, number, cm.sup.-1 Absorb. cm.sup.-1 Absorb. cm.sup.-1 Absorb. cm.sup.-1 Absorb. cm.sup.-1 Absorb. 12493 3.61 10792 3.64 9091 4.37 7390 3.21 5689 3.18 12489 3.56 10788 3.65 9087 4.28 7386 3.21 5685 3.20 12485 3.52 10784 3.65 9084 4.25 7383 3.21 5682 3.23 12482 3.48 10781 3.62 9080 4.30 7379 3.21 5678 3.24 12478 3.51 10777 3.61 9076 4.42 7375 3.20 5674 3.24 12474 3.56 10773 3.62 9072 4.48 7371 3.20 5670 3.23 12470 3.57 10769 3.64 9068 4.41 7367 3.20 5666 3.19 12466 3.56 10765 3.64 9064 4.36 7363 3.20 5662 3.15 12462 3.58 10761 3.67 9060 4.36 7359 3.21 5658 3.09 12458 3.60 10757 3.70 9057 4.37 7356 3.21 5655 3.03 12455 3.60 10754 3.68 9053 4.35 7352 3.21 5651 2.96 12451 3.65 10750 3.61 9049 4.36 7348 3.21 5647 2.90 12447 3.74 10746 3.58 9045 4.38 7344 3.21 5643 2.84 12443 3.72 10742 3.60 9041 4.45 7340 3.20 5639 2.78 12439 3.68 10738 3.62 9037 4.52 7336 3.20 5635 2.72 12435 3.67 10734 3.64 9033 4.51 7332 3.19 5631 2.66 12431 3.63 10730 3.66 9030 4.42 7329 3.19 5628 2.60 12428 3.60 10727 3.68 9026 4.34 7325 3.18 5624 2.54 12424 3.57 10723 3.68 9022 4.32 7321 3.18 5620 2.49 12420 3.51 10719 3.67 9018 4.34 7317 3.18 5616 2.44 12416 3.50 10715 3.66 9014 4.37 7313 3.18 5612 2.39 12412 3.57 10711 3.67 9010 4.41 7309 3.18 5608 2.35 12408 3.59 10707 3.66 9006 4.45 7305 3.17 5604 2.31 12404 3.54 10703 3.65 9003 4.44 7302 3.17 5601 2.28 12401 3.57 10700 3.64 8999 4.43 7298 3.17 5597 2.26 12397 3.68 10696 3.62 8995 4.49 7294 3.17 5593 2.24 12393 3.70 10692 3.60 8991 4.55 7290 3.17 5589 2.22 12389 3.63 10688 3.60 8987 4.57 7286 3.18 5585 2.21 12385 3.58 10684 3.61 8983 4.57 7282 3.18 5581 2.20 12381 3.58 10680 3.64 8979 4.58 7278 3.18 5577 2.20 12377 3.57 10676 3.67 8976 4.58 7275 3.18 5574 2.19 12374 3.57 10673 3.68 8972 4.55 7271 3.18 5570 2.18 12370 3.57 10669 3.68 8968 4.48 7267 3.18 5566 2.18 12366 3.56 10665 3.67 8964 4.46 7263 3.18 5562 2.17 12362 3.55 10661 3.65 8960 4.49 7259 3.19 5558 2.17 12358 3.56 10657 3.64 8956 4.52 7255 3.19 5554 2.16 12354 3.56 10653 3.65 8952 4.53 7251 3.19 5550 2.15 12350 3.54 10649 3.67 8949 4.55 7248 3.19 5547 2.15 12347 3.51 10646 3.69 8945 4.59 7244 3.19 5543 2.14 12343 3.50 10642 3.69 8941 4.62 7240 3.19 5539 2.13 12339 3.53 10638 3.69 8937 4.65 7236 3.19 5535 2.13 12335 3.60 10634 3.68 8933 4.69 7232 3.19 5531 2.12 12331 3.64 10630 3.66 8929 4.73 7228 3.19 5527 2.12 12327 3.59 10626 3.64 8925 4.77 7224 3.19 5523 2.12 12323 3.54 10622 3.66 8922 4.86 7221 3.19 5520 2.12 12320 3.57 10619 3.68 8918 4.84 7217 3.19 5516 2.12 12316 3.68 10615 3.66 8914 4.75 7213 3.19 5512 2.12 12312 3.68 10611 3.62 8910 4.82 7209 3.20 5508 2.12 12308 3.57 10607 3.61 8906 4.98 7205 3.20 5504 2.12 12304 3.50 10603 3.64 8902 5.07 7201 3.20 5500 2.12 12300 3.48 10599 3.70 8898 4.85 7197 3.20 5496 2.12 12296 3.50 10595 3.75 8895 4.72 7194 3.20 5493 2.11 12293 3.60 10592 3.75 8891 4.68 7190 3.21 5489 2.11 12289 3.66 10588 3.72 8887 4.79 7186 3.21 5485 2.10 12285 3.64 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7988 4.25 6287 1.85 4586 1.68 11386 4.11 9685 3.72 7984 4.26 6283 1.85 4582 1.67 11382 4.01 9681 3.72 7980 4.26 6279 1.85 4578 1.67 11378 4.05 9678 3.71 7977 4.24 6276 1.84 4575 1.66 11375 4.04 9674 3.71 7973 4.20 6272 1.84 4571 1.65 11371 4.02 9670 3.72 7969 4.18 6268 1.84 4567 1.64 11367 3.97 9666 3.72 7965 4.18 6264 1.84 4563 1.64 11363 3.93 9662 3.71 7961 4.19 6260 1.83 4559 1.63 11359 3.93 9658 3.7 7957 4.19 6256 1.83 4555 1.63 11355 3.99 9654 3.70 7953 4.17 6252 1.83 4551 1.63 11351 4.09 9651 3.71 7950 4.15 6249 1.82 4548 1.64 11348 4.18 9647 3.71 7946 4.15 6245 1.82 4544 1.64 11344 4.19 9643 3.69 7942 4.16 6241 1.82 4540 1.65 11340 4.16 9639 3.67 7938 4.18 6237 1.82 4536 1.65 11336 4.16 9635 3.67 7934 4.18 6233 1.81 4532 1.66 11332 4.07 9631 3.70 7930 4.16 6229 1.81 4528 1.67 11328 3.96 9627 3.73 7926 4.13 6225 1.81 4524 1.68 11324 3.94 9624 3.72 7923 4.10 6222 1.81 4521 1.69 11321 3.95 9620 3.70 7919 4.07 6218 1.80 4517 1.70 11317 4.01 9616 3.68 7915 4.07 6214 1.80 4513 1.71 11313 4.07 9612 3.68 7911 4.09 6210 1.80 4509 1.73 11309 4.00 9608 3.68 7907 4.09 6206 1.80 4505 1.74 11305 3.89 9604 3.70 7903 4.07 6202 1.79 4501 1.76 11301 3.84 9600 3.72 7899 4.05 6198 1.79 4497 1.78 11297 3.88 9597 3.72 7896 4.05 6195 1.79 4494 1.8 11294 3.97 9593 3.71 7892 4.06 6191 1.79 4490 1.83 11290 4.03 9589 3.70 7888 4.05 6187 1.79 4486 1.85 11286 3.99 9585 3.71 7884 4.03 6183 1.79 4482 1.88 11282 3.89 9581 3.71 7880 4.02 6179 1.79 4478 1.92 11278 3.86 9577 3.70 7876 4.01 6175 1.78 4474 1.96 11274 3.87 9573 3.70 7872 3.99 6171 1.78 4470 2.00 11270 3.85 9570 3.72 7869 3.97 6168 1.78 4467 2.05 11267 3.83 9566 3.74 7865 3.97 6164 1.78 4463 2.11 11263 3.85 9562 3.72 7861 3.97 6160 1.78 4459 2.17 11259 3.85 9558 3.71 7857 3.96 6156 1.78 4455 2.25 11255 3.84 9554 3.72 7853 3.96 6152 1.78 4451 2.35 11251 3.82 9550 3.74 7849 3.96 6148 1.78 4447 2.46 11247 3.82 9546 3.74 7845 3.96 6144 1.79 4443 2.59 11243 3.82 9543 3.74 7842 3.95 6141 1.79 4440 2.76 11240 3.81 9539 3.74 7838 3.95 6137 1.79 4436 2.95 11236 3.78 9535 3.74 7834 3.94 6133 1.79 4432 3.19 11232 3.75 9531 3.76 7830 3.92 6129 1.79 4428 3.47 11228 3.75 9527 3.77 7826 3.91 6125 1.79 4424 3.79 11224 3.83 9523 3.77 7822 3.91 6121 1.79 4420 4.12 11220 3.95 9519 3.77 7818 3.90 6117 1.79 4416 4.45 11216 4.00 9516 3.73 7815 3.90 6114 1.79 4413 4.82 11213 3.93 9512 3.71 7811 3.89 6110 1.79 4409 5.13 11209 3.82 9508 3.71 7807 3.88 6106 1.79 4405 5.19 11205 3.79 9504 3.73 7803 3.88 6102 1.79 4401 5.15 11201 3.87 9500 3.76 7799 3.88 6098 1.79 4397 5.10 11197 3.95 9496 3.78 7795 3.88 6094 1.79 4393 5.05 11193 3.89 9492 3.78 7791 3.88 6090 1.79 4389 5.05 11189 3.79 9489 3.77 7788 3.87 6087 1.79 4386 5.09 11186 3.72 9485 3.75 7784 3.86 6083 1.79 4382 5.20 11182 3.74 9481 3.73 7780 3.84 6079 1.79 4378 5.34 11178 3.79 9477 3.73 7776 3.84 6075 1.79 4374 5.39 11174 3.81 9473 3.75 7772 3.83 6071 1.78 4370 5.20 11170 3.80 9469 3.77 7768 3.82 6067 1.78 4366 5.05 11166 3.80 9465 3.77 7764 3.81 6063 1.78 4362 5.07 11162 3.78 9462 3.76 7761 3.80 6060 1.78 4359 5.26 11159 3.74 9458 3.76 7757 3.79 6056 1.79 4355 5.26 11155 3.68 9454 3.76 7753 3.79 6052 1.79 4351 5.05 11151 3.63 9450 3.76 7749 3.79 6048 1.79 4347 4.98 11147 3.62 9446 3.77 7745 3.78 6044 1.79 4343 5.11 11143 3.64 9442 3.78 7741 3.78 6040 1.80 4339 5.29 11139 3.66 9438 3.78 7737 3.78 6036 1.80 4335 5.32 11135 3.64 9435 3.77 7734 3.77 6033 1.81 4332 5.36 11132 3.61 9431 3.76 7730 3.76 6029 1.82 4328 5.40 11128 3.60 9427 3.76 7726 3.75 6025 1.82 4324 5.28 11124 3.64 9423 3.77 7722 3.74 6021 1.83 4320 5.13 11120 3.65 9419 3.78 7718 3.73 6017 1.84 4316 4.99 11116 3.63 9415 3.78 7714 3.72 6013 1.86 4312 4.95 11112 3.60 9411 3.80 7710 3.72 6009 1.87 4308 4.95 11108 3.56 9408 3.81 7707 3.72 6006 1.88 4305 4.95 11105 3.54 9404 3.82 7703 3.7 6002 1.89 4301 4.95 11101 3.53 9400 3.83 7699 3.68 5998 1.91 4297 4.97 11097 3.52 9396 3.84 7695 3.66 5994 1.93 4293 5.01 11093 3.50 9392 3.83 7691 3.65 5990 1.94 4289 5.06 11089 3.50 9388 3.83 7687 3.65 5986 1.96 4285 5.10 11085 3.51 9384 3.84 7683 3.65 5982 1.98 4281 5.17 11081 3.52 9381 3.86 7680 3.65 5979 2.00 4278 5.37 11078 3.54 9377 3.87 7676 3.64 5975 2.02 4274 5.28 11074 3.54 9373 3.88 7672 3.63 5971 2.04 4270 5.36 11070 3.51 9369 3.89 7668 3.63 5967 2.07 4266 5.34 11066 3.50 9365 3.91 7664 3.63 5963 2.09 4262 5.21 11062 3.52 9361 3.92 7660 3.62 5959 2.11 4258 5.13 11058 3.53 9357 3.91 7656 3.61 5955 2.14 4254 5.15 11054 3.53 9354 3.9 7653 3.60 5952 2.17 4251 5.16 11051 3.52 9350 3.89 7649 3.60 5948 2.20 4247 5.23 11047 3.52 9346 3.91 7645 3.59 5944 2.24 4243 5.21 11043 3.51 9342 3.94 7641 3.59 5940 2.28 4239 5.19 11039 3.50 9338 3.99 7637 3.57 5936 2.34 4235 5.27 11035 3.50 9334 4.02 7633 3.56 5932 2.40 4231 5.24 11031 3.52 9330 4.02 7629 3.56 5928 2.48 4227 5.09 11027 3.53 9327 4.01 7626 3.55 5925 2.58 4224 5.08 11024 3.52 9323 4.01 7622 3.54 5921 2.68 4220 5.19 11020 3.53 9319 4.04 7618 3.54 5917 2.79 4216 5.39 11016 3.52 9315 4.06 7614 3.53 5913 2.89 4212 5.46 11012 3.50 9311 4.05 7610 3.53 5909 2.98 4208 5.34 11008 3.49 9307 4.06 7606 3.53 5905 3.03 4204 5.23 11004 3.50 9303 4.09 7602 3.52 5901 3.06 4200 5.14 11000 3.52 9300 4.10 7599 3.51 5898 3.07 4197 5.13 10997 3.54 9296 4.10 7595 3.50 5894 3.09 4193 5.10 10993 3.53 9292 4.11 7591 3.50 5890 3.12 4189 5.02 10989 3.52 9288 4.11 7587 3.49 5886 3.17 4185 5.03 10985 3.51 9284 4.11 7583 3.48 5882 3.25 4181 5.07 10981 3.51 9280 4.10 7579 3.48 5878 3.34 4177 5.09 10977 3.53 9276 4.10 7575 3.48 5874 3.44 4173 5.09 10973 3.55 9273 4.14 7572 3.47 5871 3.52 4170 5.14 10970 3.56 9269 4.18 7568 3.46 5867 3.57 4166 5.22 10966 3.55 9265 4.17 7564 3.46 5863 3.58 4162 5.26 10962 3.53 9261 4.17 7560 3.45 5859 3.57 4158 5.27 10958 3.53 9257 4.17 7556 3.44 5855 3.55 4154 5.33 10954 3.56 9253 4.17 7552 3.44 5851 3.53 4150 5.35 10950 3.60 9249 4.18 7548 3.43 5847 3.52 4146 5.29 10946 3.60 9246 4.20 7545 3.42 5844 3.53 4143 5.25 10943 3.58 9242 4.19 7541 3.41 5840 3.54 4139 5.27 10939 3.57 9238 4.19 7537 3.41 5836 3.58 4135 5.34 10935 3.59 9234 4.24 7533 3.40 5832 3.63 4131 5.21 10931 3.59 9230 4.38 7529 3.40 5828 3.69 4127 5.14 10927 3.59 9226 4.44 7525 3.40 5824 3.75 4123 5.07 10923 3.56 9222 4.30 7521 3.39 5820 3.82 4119 4.99 10919 3.53 9219 4.20 7518 3.38 5817 3.89 4116 4.96 10916 3.51 9215 4.21 7514 3.37 5813 3.96 4112 5.02 10912 3.51 9211 4.27 7510 3.36 5809 4.02 4108 5.19 10908 3.51 9207 4.33 7506 3.36 5805 4.07 4104 5.42 10904 3.52 9203 4.37 7502 3.35 5801 4.10 4100 5.49 10900 3.53 9199 4.35 7498 3.35 5797 4.11 4096 5.37 10896 3.54 9195 4.31 7494 3.34 5793 4.09 4092 5.28 10892 3.57 9192 4.3 7491 3.33 5790 4.07 4089 5.20 10889 3.59 9188 4.29 7487 3.33 5786 4.04 4085 5.09 10885 3.57 9184 4.30 7483 3.32 5782 3.99 4081 5.01 10881 3.56 9180 4.32 7479 3.32 5778 3.93 4077 4.97 10877 3.58 9176 4.32 7475 3.31 5774 3.86 4073 4.96 10873 3.61 9172 4.28 7471 3.31 5770 3.76 4069 4.99 10869 3.62 9168 4.22 7467 3.30 5766 3.66 4065 5.02 10865 3.62 9165 4.17 7464 3.29 5763 3.55 4062 5.01 10862 3.64 9161 4.16 7460 3.29 5759 3.46 4058 5.15 10858 3.64 9157 4.19 7456 3.28 5755 3.37 4054 5.36 10854 3.63 9153 4.23 7452 3.28 5751 3.28 4050 5.40 10850 3.62 9149 4.27 7448 3.27 5747 3.21 4046 5.31 10846 3.64 9145 4.34 7444 3.27 5743 3.14 4042 5.20 10842 3.68 9141 4.41 7440 3.26 5739 3.09 4038 5.14 10838 3.71 9138 4.43 7437 3.26 5736 3.05 4035 5.05 10835 3.70 9134 4.40 7433 3.25 5732 3.03 4031 4.95 10831 3.66 9130 4.39 7429 3.25 5728 3.02 4027 4.93 10827 3.64 9126 4.37 7425 3.24 5724 3.02 4023 5.05 10823 3.64 9122 4.29 7421 3.24 5720 3.03 4019 5.23 10819 3.65 9118 4.27 7417 3.23 5716 3.04 4015 5.32 10815 3.67 9114 4.31 7413 3.23 5712 3.05 4011 5.37 10811 3.68 9111 4.34 7410 3.22 5709 3.06 4008 5.14 10808 3.66 9107 4.34 7406 3.22 5705 3.08 4004 4.88 10804 3.63 9103 4.37 7402 3.21 5701 3.10 4000 4.81 10800 3.62 9099 4.43 7398 3.21 5697 3.12 10796 3.62 9095 4.44 7394 3.21 5693 3.15
TABLE-US-00005 TABLE 5 Conventional Calculated Crude Oil AD Value AD Description Unit Assay Value (Equation (4) Naphtha, Aro W % 11.0 11.0 Naphtha, H W % 14.7 14.7 Naphtha, P W % 75.8 75.9 Naphtha, S ppmw 876 876 Naphtha, ON Unitless 52.5 52.2 GO, AP ° C. 66.0 65.8 GO, CN Unitless 59.5 59.4 GO, CP ° C. −10.0 −10.0 GO, N ppmw 71.2 98.5 GO, S ppmw 13,090 13,341 GO, Kinematic Viscosity @40° C. cSt 2.9 2.9 GO, PP ° C. −9.0 −9.2 VGO, N ppmw 617 617 VGO, S ppmw 28,800 28,800 VR, MCR W % 12.4 12.4 VR, S ppmw 52,700 52,700 Oil Sample, C5A W % 1.4 1.4 Oil Sample, MCR W % 6.2 6.2 Oil Sample, PP ° C. −15.0 −15.9 Oil Sample, Kinematic Viscosity @100° C. cSt 11.8 11.8 Oil Sample, Kinematic Viscosity @70° C. cSt 21.7 21.6 Oil Sample, N ppmw 829 835 Oil Sample, S ppmw 30,000 29,490 Oil Sample, TAN mg KOH/100 g 0.1 0.1 Oil Sample, Aro W % 20.2 21.2