Next Article in Journal
On the Potential of Power Generation from Thermoelectric Generators in Gas Turbine Combustors
Previous Article in Journal
Large Eddy Simulation of Turbulent Attached Cavitating Flows around Different Twisted Hydrofoils
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

Comparing Crude Oils with Different API Gravities on a Molecular Level Using Mass Spectrometric Analysis. Part 2: Resins and Asphaltenes

by
Jandyson M. Santos
1,2,
Alessandro Vetere
2,
Alberto Wisniewski, Jr.
3,
Marcos N. Eberlin
1,4 and
Wolfgang Schrader
2,*
1
ThoMSon Mass Spectrometry Laboratory, Institute of Chemistry, University of Campinas-UNICAMP, Campinas, 13083-970 São Paulo, Brazil
2
Max-Planck-Institut für Kohlenforschung, Kaiser-Wilhelm-Platz 1, D-45470 Mülheim an der Ruhr, Germany
3
Department of Chemistry, Federal University of Sergipe-UFS, São Cristóvão, 49100-000 Sergipe, Brazil
4
Mackenzie Presbiterian University, 01302-907 São Paulo, SP, Brazil
*
Author to whom correspondence should be addressed.
Energies 2018, 11(10), 2767; https://doi.org/10.3390/en11102767
Submission received: 22 May 2018 / Revised: 4 July 2018 / Accepted: 17 September 2018 / Published: 16 October 2018
(This article belongs to the Section L: Energy Sources)

Abstract

:
The combination of fractionation methods for crude oils, such as saturate, aromatic, resin and asphaltene (SARA) fractionation, in combination with analysis by Fourier transform ion cyclotron resonance mass spectrometry (FT-ICR MS) has been used for reducing the complexity and improving the characterization of crude oils. We have used the FT-ICR MS techniques in conjunction with electrospray ionization (ESI(±)) and atmospheric pressure photoionization (APPI(+)) to find trends between MS data of SARA fractions of crude oils with different American Petroleum Institute (API) gravities from the Sergipe-Alagoas basin (Brazil), focusing on the resin and asphaltene fractions. For the first time, an adaptation of the SARA fractionation has been performed to obtain a second resin fraction, which presented compounds with an intermediate aromaticity level between the first resins and asphaltene fraction. Both the first and second resin and the asphaltene fractions were studied on a molecular level using multiple ionization techniques and FT-ICR MS to find a direct relationship between the API gravities of a heavy, medium and light crude oil. For the FT-ICR MS data and the API gravities an aromaticity tendency was found. The data show that the use of SARA fractionation with FT-ICR MS offers a tool for comprehensive characterization of individual fractions and selective chemical characterization of the components in crude oils.

1. Introduction

Crude oil is a complex chemical mixture used to produce fuels, derivatives and chemicals. As a result of the complexity, analytical techniques with high resolving power are necessary to characterize and understand its chemical composition, which may include paraffinic chains, naphthenic and aromatic structures [1].
The quality of crude oils in primary processing is evaluated by physical properties such as American Petroleum Institute (API) gravity [2]. The API gravity has an important impact on field development decisions and the economic value of crude oils. It strongly affects the economic viability of producing fields, since, in addition to oil value, it aids in the design of the equipment used in exploration and field productivity [2,3].
Different fractionation methods have been developed and used to characterize crude oils in the form of specific fractions [4]. A simple scheme which has been used for decades to separate crude oil components into fractions of saturates, aromatics, resins and asphaltenes depending on their solubilities, is called SARA fractionation [5]. In SARA fractionation the initial step is the removal of asphaltenes using a nonpolar solvent, while the remaining fraction, named maltenes, is further separated into saturates, aromatics and resins [6]. Resin and asphaltene fractions constitute the most complex part because of a high abundance of heteroatoms (N, O and S). The resin fraction represents the most polar compounds in crude oils which may include both hydrogen-rich and hydrogen-deficient molecules, i.e., a mixture of saturated and aromatic compounds [7]. Meanwhile, asphaltenes comprise hydrocarbons and components with high numbers of heteroatoms, which contain highly condensed aromatic rings substituted with aliphatic chains [6]. The asphaltenes are reported to be maturation products of the resins. If this is the case, it indicates that one of the maturation processes involves aromatization of the nonaromatic portions of the resin [8]. Additionally, it should be expected that the transition from resin to asphaltene is fluid and that a continuum of compounds is to be found. The chemical constituents of asphaltenes and resins are quite important to determine the probability of solid-phase deposition, a major problem in the production, refining and transportation of oil [9].
The SARA fractionation of crude oils has been described in the literature in conjunction with different analytical techniques, such as thin-layer chromatography with flame-ionization detection (TLC-FID) [10], high-performance liquid chromatography (HPLC) [11], gel permeation chromatography (GPC) [12], gas chromatography mass spectrometry (GC/MS) [13] and Fourier transform ion cyclotron resonance mass spectrometry (FT-ICR MS) [14,15,16]. FT-ICR MS has shown to be an appropriate tool to provide sufficient information about the individual elemental composition (CcHhNnOoSs) of species present in complex samples, because it allows differentiating between thousands of species within a single mass spectrum [17,18,19]. Recently, a review article about crude oil analysis and MS techniques has shown that the SARA fractionation reduces matrix effects and ionic suppression for the analysis with FT-ICR MS, allowing a comprehensive characterization of the constituents present in the fractions in comparison with the corresponding crude oil [20]. Hence, the SARA fractionation can be used as a sample simplification step to reduce the complexity of crude oils, which results in a higher yield of assigned signals [15,18,21].
Shi and co-workers [22] have reported an investigation of neutral nitrogen and oxygen compounds in crude oil and its SARA fractions using electrospray ionization (ESI) FT-ICR MS. Besides, atmospheric pressure laser ionization (APLI) in conjunction with FT-ICR MS has been applied to show the potential of SARA fractionation method as a sample-simplification tool that allows a reduction of components present during the measurement [15]. An oil spill site has been studied at different weathering stages and compared to in vitro photo-degradation experiments by SARA fractionation and FT-ICR MS for a more detailed comparison on the molecular level [23].
In the first part of this work [24] we have performed a detailed characterization of crude oils with different API gravities (API30, API23 and API16) on a molecular level from FT-ICR MS data using different ionization techniques. Herein, for the first time the FT-ICR MS data obtained using the perhaps two most complementary atmospheric pressure ionization techniques ESI(±) and APPI(+) were processed in terms of class, double bond equivalents (DBE) and carbon number to try to find parameters that can indicate tendencies for the FT-ICR MS data of the resin and asphaltene fractions obtained from these three crude oils. We also have investigated an adaptation on the SARA fractionation to obtain a second resin fraction unprecedented in the literature.

2. Results and Discussion

2.1. Crude Oil Properties, SARA Fractionation and Elemental Analysis

In Table 1 the major physical and chemical properties are summarized including the classification and the elemental analysis ratio for the three crude oil samples used for this study. According to their API gravity the samples were classified as light (API30), medium (API23) and heavy (API16) crude oils [25]. Note that, as expected [1], density inversely correlates to the API gravities. In addition, Table 1 indicates a trend between API gravity and H/C ratios. Lower H/C ratios show higher aromaticity levels for crude oils. The same is true for direct tendency between the N/C ratios and API gravities, whereas no tendency was found for the O/C and S/C ratios.
These three crude oils were then fractionated using a modified SARA fractionation scheme. The first step was the removal of the volatile compounds followed by the usual SARA fractionation. Additionally, it was found that at the end of the SARA fractionation, especially for heavy crude oils, still quite a lot of material was remaining on the alumina column which was not eluting using methanol as mobile phase. Therefore, we have added an additional step by using ethyl acetate as mobile phase to remove this material from the column. This fraction was analyzed and studied here in detail as resin2 fraction. In Figure 1 the mass balance of the SARA fractions from the three crude oils with different API gravities is illustrated. We have obtained a final recovery of 95% (w/w), 93% (w/w) and 87% (w/w) respectively for the API30, API23 and API16 oils, and some tendencies between SARA fraction with API gravity were observed. Note that the volatile and saturate fraction abundances are directly proportional with API gravity, because these fractions are constituted mostly by light compounds. For the resin1, resin2 and asphaltene fractions, which represent the fraction with higher polar/aromatic content, the tendency was inversely proportional.
Table 2 lists the major physical and chemical properties, classification and element ratios for the resin1, resin2 and asphaltene fractions obtained from the three crude oils. The elemental analysis for the same fraction among the samples gives some trends towards API gravity. The H/C and N/C ratios directly correlate with API gravity for the resin1 and asphaltene fractions, and an inverse tendency was found for the resin2 fraction, whereas no trends were obtained for the O/C and S/C ratio. Considering different fractions of the same crude oil, we have found the lower H/C ratio for asphaltenes, which shows that these exhibits the highest aromaticity among the fractions studied. Also the S/C ratio is higher in asphaltene fractions.

2.2. ESI(+) FT-ICR MS

The class distribution as determined from assigned elemental compositions detected by positive mode electrospray ionization (ESI(+)) FT-ICR MS for resin1, resin2 and asphaltene fractions (for the full spectra see Figures S1–S3) obtained from the different crude oils are illustrated in Figure 2.
Being the most basic components, easily detected via ESI(+), the most abundant heteroatom class for resin1, resin2 and asphaltene fractions in all crude oils was N[H]. A tendency of the N[H]-class abundance with API gravity was determined for the resin1 and resin2 fractions of the three crude oils, whereas for the asphaltene fractions the N2[H], NO[H] and N2O[H] directly correlate and OS[H] inversely correlates with API gravity, respectively.
To further investigate trends of FT-ICR MS data with API gravity, we calculated the average DBE values (DBEavg) for the most abundant N[H]-class in resin1, resin2 and asphaltene fractions, as listed in Table 3. The DBEavg indicates the aromaticity level for a specific class from the DBE distribution data obtained by FT-ICR MS analysis [7]. The data show that the DBEavg inversely correlates with API gravity for all fractions. We have previously studied the whole crude oils [24] and the same tendencies were obtained, which suggests that the resin1, resin2 and asphaltene fractions are mainly responsible for the characteristics of the crude oil in regard to the API gravity value.
The concept of planar limit was applied on the data of the different classes of both resin and asphaltene fractions [26]. The planar limit equation is calculated from the DBE versus carbon count plot by linear regression of the data points given by the highest DBE values observed for each carbon number. A higher slope indicates a higher aromaticity with an increasingly condensed π-system. In Table 3 the slope (sl) of the planar limit equation for the N[H]-class found in resin1, resin2 and asphaltene fractions is summarized. The slope value inversely correlates with the API gravity for all fractions, as does the average DBE. The DBEavg and the slope show an aromaticity tendency order independent of the fraction, in the following order: API16 > API23 > API30.
Regarding the N[H]-class within the fractions of the same crude oil, DBEavg and slope increase from resin1 to asphaltene, which shows that the asphaltene fraction contains the highest aromatic compounds in crude oil. The aromaticity distribution of the resin2 fraction falls between the resin1 and asphaltene fractions rounding out the continuum of compounds in the carbon space.

2.3. ESI(−) FT-ICR MS

Figure 3 illustrates the class distribution as determined from assigned elemental compositions as detected by ESI(−) FT-ICR MS for resin1, resin2 and asphaltene fractions (the full spectra are shown in Figures S4–S6) obtained from crude oils with different API gravities. For the resin1 fraction the most abundant classes in the three crude oils (API30, API23 and API16) were NO[H], N[H] and O[H], respectively. The abundances of classes containing nitrogen (N[H], NO[H] and NO2[H] classes) directly correlates with API gravity, whereas an inverse tendency of O[H]-class with API gravity was found. For the resin2 fraction the most abundant class found in the API30 and API23 crudes was again N[H], whereas the NO[H]-class was dominant in the API16 crude, indicating no direct trend of class abundance with API gravity.
For the asphaltene fraction N[H] was found to be most abundant in the API30 crude, whereas the O2[H]-class dominates in the API23 and API16 crudes. The nitrogen dominated classes (N[H], N2[H], N2O[H] and NO[H]) directly correlate with API gravity, whereas the classes exceeding oxygen (O[H], O2[H], O3[H] and NO2[H]) inversely correlate. These trends can be due to the oxygenation of compounds during the thermal evolution into heavy crude oils, which are associated with the presence of oxygenated compounds that are present in high abundance and due to high acidic characteristic given by the oxygen compounds [27]. For instance, compounds of NO[H]-class with higher intensities in the asphaltenes of light crude oil (API30) may undergo oxygenation reactions and form compounds of NO2[H]-class with higher intensity in heavy crude oils (API16).
We also have found trends between DBEavg and API gravity. In Table 4 DBEavg for the most abundant class of resin1, resin2 and asphaltene fractions obtained from ESI(−) FT-ICR MS data is listed. The DBEavg inversely correlates with the API gravity for all fractions, as observed for N[H] from ESI(+) data.
We also applied the planar limit concept to the data from the most abundant classes present in resin1, resin2 and asphaltene fractions obtained from ESI(−) FT-ICR MS data (Table 3). The slope also inversely correlates with API gravity for all fractions.
Then, for DBEavg and slope we have obtained the same aromaticity tendency shown for the ESI(+) data independent of the fractions analyzed, in the following order: API16 > API23 > API30, which suggests that the compounds present in resin1, resin2 and asphaltene fractions seem to be mainly responsible for the API gravity of the crude oils, as shown via ESI(+) data.

2.4. APPI(+) FT-ICR MS

Figure 4 shows the class distribution determined from assigned elemental compositions as detected by APPI(+) FT-ICR MS for resin1, resin2 and asphaltene fractions (the full spectra are displayed in Figures S7–S9) obtained from crude oils with different API gravities.
The plots reveal the N[H] (and N) class to be most abundant in the resin1 and resin2 fractions, whereas the HC[H] (and HC) class is the most abundant in the asphaltene fraction. In the first part of this study, the APPI(+) FT-ICR MS data of the whole crude oil are dominated by the HC[H] (and HC) class [24]. The resin1 and resin2 fractions represent the most polar compounds present in crude oils, thus being relatively enriched in N-containing species, whereas the APPI(+) data of the whole crude oil emphasizes the main portion of mainly aromatic hydrocarbons. The SARA fractionation in combination with FT-ICR MS for the characterization of its individual fractions thus allows the reduction of the complexity and a more complete chemical characterization of the components of crude oils.
For the resin1 fraction we have found a direct tendency of NO, O, O[H], O2 and O2[H] classes with API gravity, whereas the N[H]-class inversely correlates with API gravity. For resin2 the N[H]-class also inversely correlates, whereas N, NO, NO[H] and O classes directly correlate with API gravity. For the asphaltene fraction, no trends were found as also shown by Pereira and co-workers [28].
Table 5 summarizes the DBEavg for the most abundant classes for resin1, resin2 and asphaltene fractions obtained from APPI(+) FT-ICR MS data. For all fractions DBEavg inversely correlates with API gravity, as was also shown for the ESI(+) and ESI(−) data. Table 5 also shows the slope of the planar limit equation, which also inversely correlates with the API gravity. Then, from the average DBE and slope obtained by APPI(+) FT-ICR MS data of resin1, resin2 and asphaltene fractions we have found again the aromaticity tendency in the following order: API16 > API23 > API30.

2.5. Combining ESI(±) Plus APPI(+) to SARA Fraction Analysis

For a good representation of all the different data sets a number of different ways can be used. Here, the studies show that the combination of ESI(±) plus APPI(+) FT-ICR MS data is capable of capturing the broadest composition profile of the compounds present in crude oil SARA fractions. Figure 5A shows a comparison between ESI(±) and APPI(+) FT-ICR MS data for the N and N[H] classes of the resin2 fraction obtained from the API16 oil as an example. The ESI(+) data display by far the best sensitivity for the N[H]-class whereas the broadest DBE distribution from DBE 5 to 35 was found when using APPI(+). ESI(−) shows the highest abundances at higher DBE, which reinforces that the different ionization methods offer complementary data and together yield a more comprehensive molecular analysis of crude oils from SARA fractions [29,30].
Another interesting comparison is illustrated for the same classes throughout the SARA fractions. Figure 5B shows the DBE distributions of the N[H]-class for resin1, resin2 and asphaltene fractions obtained from the API16 crude oil using ESI(+) FT-ICR MS. Note that the DBE distributions are clearly different among the fractions. The resin1 fraction displays by far the highest intensity for the N[H]-class, which is centered around DBE 9, whereas the resin2 and asphaltene fractions present the highest intensity centered around DBE 12 and 26, respectively. Figure 5C shows a comparison of DBE distribution plots for the NO[H]-class among the different fractions. For the resin1 fraction the DBE distribution is centered around 13, and around 19 and 26 for the resin2 and asphaltene fractions, respectively. We can conclude that the distinct DBE distributions for the N[H] and NO[H] classes show an order of aromaticity among the fractions, in the following order: asphaltene > resin2 > resin1.
The SARA methodology described herein to obtain the second resin fraction (resin2) shows that the resin2 fraction presents a characteristic compound distribution with an intermediate aromaticity level between that found in the resin1 and asphaltene fractions. This finding favors the expectation stated above, that a gradual trend exists between the classically reported resin fraction and asphaltenes.
The potential of the SARA fractionation in conjunction with multiple ionization techniques and FT-ICR MS is shown in Figure 6 from the number of assigned elemental compositions. Summed over the API16, API23 and API30 oils and all ionization techniques we have obtained a total of 46,899, 45,945 and 49,326 assignments for the resin1, resin2 and asphaltene fractions, respectively. This is approximately 4 times higher than compared to the number of formula assignments found for the whole crude oil, as shown in the first part of this work [24]. The number of assigned elemental compositions in the resin2 and asphaltene fractions is higher than compared to the resin1 fraction or the whole crude oil, which shows that the second resin fraction is an important innovation into the SARA procedure, especially for heavy crude oils.
We have constructed Venn diagrams, as illustrated in Figure 7 for resin2 as a representative fraction obtained from the heavy crude oil sample (API16) to show the complementarity of ESI(±) plus APPI(+) FT-ICR MS data (for a full spectrum see Figure S10). The number within each circle represents the amount of elemental compositions assigned uniquely for each technique whereas the number within the overlap regions represents the amount of compositions that have been co-assigned from the corresponding ionization techniques. Note that the majority of assigned compositions (11,193, 77%) have been found exclusively by one ionization technique and just a small fraction (3378, 23%) of signals were co-assigned. The number of compositions obtained from APPI(+) greatly surpasses both ESI(+) and ESI(−). The similar amount of elemental compositions in the Venn diagram unique for each technique were also obtained for the samples API30 and API23. The Venn diagram shows that indeed the combination of ESI(±) plus APPI(+) in conjunction with FT-ICR MS and individual SARA fractions analysis provides a quite broad coverage of the overall composition of crude oils.

3. Materials and Methods

3.1. Samples and SARA Fractionation

The properties of crude oil samples used in this work were described previously [24]. Methanol was purchased from (J.T. Baker, Deventer, Netherlands), n-heptane and toluene were purchased from Merck KgaA (Darmstadt, Germany), cyclohexane from Acros (Geel, Belgium), dichloromethane and ethyl acetate were from Sigma-Aldrich (Steinheim, Germany).
For the SARA fractionation we adapted the procedure described elsewhere [15,17]. Briefly n-heptane (30 mL of per g of crude oil) was added and the mixture was refluxed for 1 h. Subsequently the mixture was cooled down and stored in the dark overnight. Then, the precipitated portion (the asphaltenes) was filtered off (Whatman, type 589.3 blue ribbon filter). The asphaltene loaded filter was placed into a Soxhlet extractor and refluxed with n-heptane for 2 h to wash off remaining maltenes. The solvent was then replaced with fresh toluene (150 mL) and the extraction proceeded until asphaltenes had been dissolved from the filter paper (24 h). The re-dissolved asphaltene fraction was rotary evaporated and afterwards dried under a continuous stream of nitrogen. The combined maltene portions were adsorbed onto activated neutral alumina (80–200 mesh, Brockmann I, Sigma-Aldrich, Steinheim, Germany) and subjected to open column chromatography (activated neutral alumina, 3 × 40 cm). Cyclohexane, cyclohexane:dichloromethane (1:1, v/v), methanol and ethyl acetate were used consecutively to elute saturates, aromatics, and two resin fractions (resin1 and resin2), respectively. The separation was monitored by UV absorbance of the effluent. For mass balance volatile compounds were determined by evaporation at 50 mbar and 40 °C.
Measurements of the first and second resin and the asphaltene fractions were performed using stock solutions in toluene of 1 mg·mL−1. These were further diluted in methanol to obtain a final solution of 0.3 mg·mL−1 in toluene:methanol. For ESI(+), formic acid was added to favor [M + H]+ ions, and for ESI(−) methanolic ammonium hydroxide was added to favor [M − H] ions. For APPI(+) no additives were added as the solvent toluene can act as a dopant for dopant assisted APPI.

3.2. Elemental Analysis

The measurements of C, H, N, and S contents of the resin1, resin2 and asphaltene fractions were obtained from a Vario Elementar CHN-Analyzer (Elementar Analysensysteme GmbH, Hanau, Germany). The O content was calculated as the difference to 100%.

3.3. FT-ICR MS Analysis

FT-ICR MS analyses were performed using a 7 T linear trap quadrupole (LTQ) FT-ICR mass spectrometer (LTQ FT Ultra, Thermo Fisher, Bremen, Germany) equipped with an ESI or APPI source. For ESI(±) a capillary voltage of +4.0 or −3.4 kV, tube lens voltage of +100 or −120 V and a capillary voltage of +35 or −40 V, respectively and a capillary temperature of 275 °C were used. Nitrogen was used as nebulization gas with a sheath gas flow of 5–10, auxiliary and sweep gas flow of 1 (arbitrary units). The sample solutions were directly infused at a flow rate of 5 μL·min−1. For APPI(+) the vaporizer temperature was set to 350 °C, with a capillary temperature of 275 °C. Tube lens voltage was +75 V. Nitrogen was used as nebulization gas with a sheath gas flow of 10–20 and auxiliary and sweep gas flow of 5 (arbitrary units). A flow rate of 20 μL·min−1 was used for direct infusion. Ionization was performed using a Kr-VUV lamp with photon emission at 10.0 and 10.6 eV (Syagen Technology, Santa Ana, CA, USA). All analyses were performed using a transient of 3 s resulting in a mass resolving power of m/∆m50% = 400,000 (FWHM at m/z 400), collecting 100 scans for each run. The data acquisition was performed in the mass range of m/z 200–1400.

3.4. Data Analysis

The FT-ICR MS data obtained were averaged by Xcalibur 2.2 software (Thermo Fischer Scientific, Bremen, Germany) and then imported to Composer software (v1.5.0, Sierra Analytics, Modesto, CA, USA) for peak assignment. Constraints for the assignment of elemental compositions were: 0 ≤ H ≤ 1000, 0 ≤ C ≤ 200, 0 ≤ N ≤ 3, 0 ≤ O ≤3, 0 ≤ S ≤3 and 0 ≤ DBE ≤ 40 with a maximum mass error of 1 ppm. (De-)protonated molecules and radical ions were distinguished and assigned separately. Then, the assignment data were transferred into sorted Excel workbooks by an in-house written algorithm for further evaluation.

4. Conclusions

A comprehensive characterization on a molecular level of resin and asphaltene fractions obtained from crude oils with different API gravities using multiple ionization techniques in conjunction with FT-ICR MS is reported. In the first part of this study, a whole crude oil was studied and trends between MS data and API gravity were found for the three samples, but the question as to whether the most polar and complex fractions were also responsible by the aromaticity and API gravity values were not answered and we are now able to answer it in this second paper. Herein different data interpretation methods were successfully applied to SARA fractions to correlate the molecular assignments from FT-ICR MS data with API gravity. An important extension of the SARA fractionation procedure is reported by adding a second resin fraction, which was important to acquire and characterize a fraction that has shown presence of compounds with an intermediate aromaticity level between the resin1 (which is obtained from the SARA fractionations commonly published in literature) and the asphaltene fractions. This is a strong indication for a compound continuum that fills the gap between classical resin and asphaltenes fractions. So it is shown that the analysis of SARA fractionation by ESI(±) plus APPI(+) and FT-ICR MS permits the characterization of individual fractions, providing a reduction in the complexity of sample and a more complete and selective chemical characterization of the components present in crude oils.

Supplementary Materials

The following is available online at https://www.mdpi.com/1996-1073/11/10/2767/s1, Figure S1: ESI(+) FT-ICR MS for the resin1 fraction obtained from crude oil with different API gravities; Figure S2: ESI(+) FT-ICR MS for the resin2 fraction obtained from crude oil with different API gravities; Figure S3: ESI(+) FT-ICR MS for the asphaltene fraction obtained from crude oil with different API gravities; Figure S4: ESI(−) FT-ICR MS for the resin1 fraction obtained from crude oil with different API gravities; Figure S5: ESI(−) FT-ICR MS for the resin2 fraction obtained from crude oil with different API gravities; Figure S6: ESI(−) FT-ICR MS for the asphaltene fraction obtained from crude oil with different API gravities; Figure S7: APPI(+) FT-ICR MS for the resin1 fraction obtained from crude oil with different API gravities; Figure S8: APPI(+) FT-ICR MS for the resin2 fraction obtained from crude oil with different API gravities; Figure S9: APPI(+) FT-ICR MS for the asphaltene fraction obtained from crude oil with different API gravities; Figure S10: ESI(+), ESI(−) and APPI(+) FT-ICR MS for resin2 fraction obtained from the heavy crude oil with API gravity of 16 (API16).

Author Contributions

W.S. and M.N.E. developed research; J.M.S. performed the experiments and analyzed the data; A.V. developed the resin2 procedure, A.W.J. contributed reagents/materials/analysis tools; J.M.S., A.V. and W.S. wrote the paper.

Funding

São Paulo Research Foundation (FAPESP) and Petróleo Brasileiro S/A (Petrobras).

Acknowledgments

The authors are grateful to FAPESP (process number 2013/19161-4 and 2015/05818-7) by the fellowships, the Petrobras (Petróleo Brasileiro S/A) for financial support and the Max-Planck-Institut für Kohlenforschung for the use of its infrastructure. Additionally, the authors thank David Stranz (Sierra Analytics, Modesto, CA) for assistance in MS-data evaluation.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Speight, J.G. The Chemistry and Technology of Petroleum, 4th ed.; CRC Press: New York, NY, USA, 2006. [Google Scholar]
  2. Filgueiras, P.R.; Sad, C.M.S.; Loureiro, A.R.; Santos, M.F.P.; Castro, E.V.R.; Dias, J.C.M.; Poppi, R.J. Determination of API gravity, kinematic viscosity and water content in petroleum by Atr-Ftir spectroscopy and multivariate calibration. Fuel 2014, 116, 123–130. [Google Scholar] [CrossRef]
  3. Abbas, O.; Rebufa, C.; Dupuy, N.; Permanyer, A.; Kister, J. PLS regression on spectroscopic data for the prediction of crude oil quality: API gravity and aliphatic/aromatic ratio. Fuel 2012, 98, 5–14. [Google Scholar] [CrossRef]
  4. Santos, J.M.; Santos, F.M.L.; Araujo, R.G.O.; Lessa, A.C.; Souza, J.P.D.; Santos, M.J.D.; Wisniewski, A. Chemical aspects of onshore crude oils from the carmópolis field, sergipe-alagoas basin, brazil: A case study on the industrial process for water-oil separation. Energy Fuels 2015, 29, 1315–1322. [Google Scholar] [CrossRef]
  5. Kharrat, A.M.; Zacharia, J.; Cherian, V.J.; Anyatonwu, A. Issues with comparing SARA methodologies. Energy Fuels 2007, 21, 3618–3621. [Google Scholar] [CrossRef]
  6. Molnárné Guricza, L.; Schrader, W. New separation approach for asphaltene investigation: Argentation chromatography coupled with ultrahigh-resolution mass spectrometry. Energy Fuels 2015, 29, 6224–6230. [Google Scholar] [CrossRef]
  7. Cho, Y.; Na, J.G.; Nho, N.S.; Kim, S.; Kim, S. Application of saturates, aromatics, resins, and asphaltenes crude oil fractionation for detailed chemical characterization of heavy crude oils by fourier transform ion cyclotron resonance mass spectrometry equipped with atmospheric pressure photoionization. Energy Fuels 2012, 26, 2558–2565. [Google Scholar]
  8. Speight, J.G. Petroleum asphaltenes—Part 1: Asphaltenes, resins and the structure of petroleum. Oil Gas Sci. Technol. 2004, 59, 467–477. [Google Scholar] [CrossRef]
  9. Riazi, M.R.; Roomi, Y.A. Compositional analysis of petroleum fractions. Am. Chem. Soc. Div. Pet. Chem. Prepr. 2001, 46, 391–394. [Google Scholar]
  10. Fan, T.; Buckley, J.S. Rapid and accurate sara analysis of medium gravity crude oils. Energy Fuels 2002, 16, 1571–1575. [Google Scholar] [CrossRef]
  11. Woods, J.R.; Kung, J.; Kingston, D.; Kotlyar, L.; Sparks, B.; McCracken, T. Canadian crudes: A comparative study of SARA fractions from a modified HPLC separation technique. Oil Gas Sci. Technol. 2008, 63, 151–163. [Google Scholar] [CrossRef]
  12. Fuhr, B.; Scott, K.; Dettman, H.; Salmon, S. Fractionation of bitumen by distillation, SARA analysis and gel permeation chromatography. Am. Chem. Soc. Div. Pet. Chem. Prepr. 2005, 50, 264–265. [Google Scholar]
  13. Herring, A.M.; Johnston, M.H.; Batzle, M.; Liberatore, M.; Dec, S.F. Using mass spectrometry to improve on the SARA analysis for a series of canadian heavy oils. In Proceedings of the ACS 2009 237th National Meeting and Exposition of the American Chemical Society, Salt Lake City, UT, USA, 22–26 March 2009. [Google Scholar]
  14. Marshall, A.G.; Rodgers, R.P. Petroleomics: The next grand challenge for chemical analysis. Acc. Chem. Res. 2004, 37, 53–59. [Google Scholar] [CrossRef] [PubMed]
  15. Gaspar, A.; Zellermann, E.; Lababidi, S.; Reece, J.; Schrader, W. Characterization of saturates, aromatics, resins, and asphaltenes heavy crude oil fractions by atmospheric pressure laser ionization fourier transform ion cyclotron resonance mass spectrometry. Energy Fuels 2012, 26, 3481–3487. [Google Scholar] [CrossRef]
  16. McKenna, A.M.; Purcell, J.M.; Rodgers, R.P.; Marshall, A.G. Heavy petroleum composition. 1. Exhaustive compositional analysis of athabasca bitumen HVGO distillates by fourier transform ion cyclotron resonance mass spectrometry: A definitive test of the boduszynski model. Energy Fuels 2010, 24, 2929–2938. [Google Scholar] [CrossRef]
  17. Molnárné Guricza, L.; Schrader, W. Electrospray ionization for determination of non-polar polyaromatic hydrocarbons and polyaromatic heterocycles in heavy crude oil asphaltenes. J. Mass Spectrom. 2015, 50, 549–557. [Google Scholar] [CrossRef] [PubMed]
  18. Panda, S.K.; Andersson, J.T.; Schrader, W. Mass-spectrometric analysis of complex volatile and nonvolatile crude oil components: A challenge. Anal. Bioanal. Chem. 2007, 389, 1329–1339. [Google Scholar] [CrossRef] [PubMed]
  19. Corilo, Y.E.; Vaz, B.G.; Simas, R.C.; Lopes Nascimento, H.D.; Klitzke, C.F.; Pereira, R.C.L.; Bastos, W.L.; Santos Neto, E.V.; Rodgers, R.P.; Eberlin, M.N. Petroleomics by EASI(±) FT-ICR MS. Anal. Chem. 2010, 82, 3990–3996. [Google Scholar] [CrossRef] [PubMed]
  20. Cho, Y.; Ahmed, A.; Islam, A.; Kim, S. Developments in FT-ICR MS instrumentation, ionization techniques, and data interpretation methods for petroleomics. Mass Spectrom. Rev. 2015, 34, 248–263. [Google Scholar] [CrossRef] [PubMed]
  21. Schrader, W.; Panda, S.K.; Brockmann, K.J.; Benter, T. Characterization of non-polar aromatic hydrocarbons in crude oil using atmospheric pressure laser ionization and fourier transform ion cyclotron resonance mass spectrometry (APLI FT-ICR MS). Analyst 2008, 133, 867–869. [Google Scholar] [CrossRef] [PubMed]
  22. Shi, Q.; Hou, D.; Chung, K.H.; Xu, C.; Zhao, S.; Zhang, Y. Characterization of heteroatom compounds in a crude oil and its saturates, aromatics, resins, and asphaltenes (SARA) and non-basic nitrogen fractions analyzed by negative-ion electrospray ionization fourier transform ion cyclotron resonance mass spectrometry. Energy Fuels 2010, 24, 2545–2553. [Google Scholar]
  23. Islam, A.; Cho, Y.; Yim, U.H.; Shim, W.J.; Kim, Y.H.; Kim, S. The comparison of naturally weathered oil and artificially photo-degraded oil at the molecular level by a combination of SARA fractionation and FT-ICR MS. J. Hazard. Mater. 2013, 263, 404–411. [Google Scholar] [CrossRef] [PubMed]
  24. Santos, J.M.; Wisniewski, A., Jr.; Eberlin, M.N.; Schrader, W. Comparing crude oils with different api gravities on a molecular level by mass spectrometric analysis. Part 1: Whole crude oil. Energies 2018, in press. [Google Scholar]
  25. National Agency of Petroleum, Natural Gas and Biofuels. Portaria N° 009 de 21 de Janeiro de 2000; National Agency of Petroleum, Natural Gas and Biofuels: Rio de Janeiro, Brazil, 2000.
  26. Cho, Y.; Kim, Y.H.; Kim, S. Planar limit-assisted structural interpretation of saturates/aromatics/resins/asphaltenes fractionated crude oil compounds observed by fourier transform ion cyclotron resonance mass spectrometry. Anal. Chem. 2011, 83, 6068–6073. [Google Scholar] [CrossRef] [PubMed]
  27. Vaz, B.G.; Silva, R.C.; Klitzke, C.F.; Simas, R.C.; Lopes Nascimento, H.D.; Pereira, R.C.L.; Garcia, D.F.; Eberlin, M.N.; Azevedo, D.A. Assessing biodegradation in the llanos orientales crude oils by electrospray ionization ultrahigh resolution and accuracy fourier transform mass spectrometry and chemometric analysis. Energy Fuels 2013, 27, 1277–1284. [Google Scholar] [CrossRef]
  28. Pereira, T.M.C.; Vanini, G.; Oliveira, E.C.S.; Cardoso, F.M.R.; Fleming, F.P.; Neto, A.C.; Lacerda, V., Jr.; Castro, E.V.R.; Vaz, B.G.; Romão, W. An evaluation of the aromaticity of asphaltenes using atmospheric pressure photoionization fourier transform ion cyclotron resonance mass spectrometry—APPI(±) FT-ICR MS. Fuel 2014, 118, 348–357. [Google Scholar] [CrossRef]
  29. Panda, S.K.; Andersson, J.T.; Schrader, W. Characterization of supercomplex crude oil mixtures: What is really in there? Angew. Chem. Int. Ed. 2009, 48, 1788–1791. [Google Scholar] [CrossRef] [PubMed]
  30. Gaspar, A.; Zellermann, E.; Lababidi, S.; Reece, J.; Schrader, W. Impact of different ionization methods on the molecular assignments of asphaltenes by FT-ICR mass spectrometry. Anal. Chem. 2012, 84, 5257–5267. [Google Scholar] [CrossRef] [PubMed]
Figure 1. Mass distribution of saturate, aromatic, resin and asphaltene (SARA) fractions for the three crude oils with different API gravities.
Figure 1. Mass distribution of saturate, aromatic, resin and asphaltene (SARA) fractions for the three crude oils with different API gravities.
Energies 11 02767 g001
Figure 2. Class distribution based on assigned elemental compositions for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using ESI(+) Fourier transform ion cyclotron resonance mass spectrometry (FT-ICR MS).
Figure 2. Class distribution based on assigned elemental compositions for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using ESI(+) Fourier transform ion cyclotron resonance mass spectrometry (FT-ICR MS).
Energies 11 02767 g002
Figure 3. Class distributions based on assigned elemental compositions for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using ESI(−) FT-ICR MS.
Figure 3. Class distributions based on assigned elemental compositions for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using ESI(−) FT-ICR MS.
Energies 11 02767 g003
Figure 4. Class distributions based on assigned elemental compositions for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using APPI(+) FT-ICR MS.
Figure 4. Class distributions based on assigned elemental compositions for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using APPI(+) FT-ICR MS.
Energies 11 02767 g004
Figure 5. Double bond equivalents (DBE) distribution plot for: (A) N and N[H] classes of the resin2 fraction obtained from API16 crude oil using ESI(+), ESI(−) and APPI(+) FT-ICR MS; (B) N[H]-class and (C) NO[H]-class of the resin1, resin2 and asphaltene fractions obtained from API16 crude oil using ESI(+) FT-ICR MS.
Figure 5. Double bond equivalents (DBE) distribution plot for: (A) N and N[H] classes of the resin2 fraction obtained from API16 crude oil using ESI(+), ESI(−) and APPI(+) FT-ICR MS; (B) N[H]-class and (C) NO[H]-class of the resin1, resin2 and asphaltene fractions obtained from API16 crude oil using ESI(+) FT-ICR MS.
Energies 11 02767 g005
Figure 6. Sum of the assigned elemental compositions obtained from ESI(+), ESI(−) and APPI(+) FT-ICR MS data of the whole crude oil (data described in Santos et al. [24]) with different API gravity and their resin1, resin2 and the asphaltene fractions.
Figure 6. Sum of the assigned elemental compositions obtained from ESI(+), ESI(−) and APPI(+) FT-ICR MS data of the whole crude oil (data described in Santos et al. [24]) with different API gravity and their resin1, resin2 and the asphaltene fractions.
Energies 11 02767 g006
Figure 7. Venn diagram showing the total amount of assigned compositions obtained from ESI(+), ESI(−) and APPI(+) FT-ICR MS data for the resin2 fraction obtained from the heavy crude oil (API16).
Figure 7. Venn diagram showing the total amount of assigned compositions obtained from ESI(+), ESI(−) and APPI(+) FT-ICR MS data for the resin2 fraction obtained from the heavy crude oil (API16).
Energies 11 02767 g007
Table 1. Major physical properties and elemental analyses ratios for the three crude oil samples.
Table 1. Major physical properties and elemental analyses ratios for the three crude oil samples.
SampleAPI30API23API16
Data
API gravity30.023.516.4
Density (g·cm−3)0.87350.90890.9530
Classification *LightMediumHeavy
H/C1.66861.58291.5588
N/C0.00600.00420.0026
O/C0.02910.01880.0363
S/C0.00130.00170.0010
* Source: ANP (2000) [25].
Table 2. Major physical and chemical properties and element ratios for the resin1, resin2 and asphaltenes (asph.) fractions obtained from crude oils with different API gravities.
Table 2. Major physical and chemical properties and element ratios for the resin1, resin2 and asphaltenes (asph.) fractions obtained from crude oils with different API gravities.
SampleAPI30API23API16
Data
Crude oil API gravity30.023.516.4
Density (g·cm−3)0.87350.90890.9530
Classification *LightMediumHeavy
Fractionresin1resin2asph.resin1resin2asph.resin1resin2asph.
H/C1.49481.33150.96401.38701.37990.94411.31641.46630.8845
N/C0.02180.00970.01450.01460.01000.01090.01350.01050.0111
O/C0.88380.02600.05060.55540.05160.08191.05590.10830.1041
S/C0.00160.00230.00560.00580.00470.00650.00230.00230.0027
* Source: ANP (2000) [25].
Table 3. Average DBE (DBEavg) and slope of planar limit equation (sl) for the N[H]-class of resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using ESI(+) FT-ICR MS.
Table 3. Average DBE (DBEavg) and slope of planar limit equation (sl) for the N[H]-class of resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using ESI(+) FT-ICR MS.
FractionResin1Resin2Asphaltene
Sample DBEavgslDBEavgslDBEavgsl
API3011.240.368713.570.378720.320.5020
API2311.420.382413.580.444420.390.5728
API1613.690.434814.280.478927.440.6207
Table 4. Average DBE (DBEavg), the slope of planar limit equation (sl) and the respective class for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using ESI(−) FT-ICR MS.
Table 4. Average DBE (DBEavg), the slope of planar limit equation (sl) and the respective class for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using ESI(−) FT-ICR MS.
FractionResin1 O[H]-ClassResin2 NO[H]-ClassAsphaltene O2[H]-Class
Sample DBEavgslDBEavgslDBEavgsl
API307.250.429820.920.388110.220.5497
API238.250.486920.980.437410.330.5517
API168.380.512821.230.465610.580.5728
Table 5. Average DBE (DBEavg), the slope of planar limit equation (sl) and the respective class for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using APPI(+) FT-ICR MS.
Table 5. Average DBE (DBEavg), the slope of planar limit equation (sl) and the respective class for the resin1, resin2 and asphaltene fractions obtained from crude oils with different API gravities using APPI(+) FT-ICR MS.
FractionResin1 N-ClassResin2 N[H]-ClassAsphaltene HC[H]-Class
Sample DBEavgslDBEavgslDBEavgsl
API3014.700.437513.690.515413.860.6413
API2314.880.449913.790.524514.480.6686
API1615.150.456014.760.550215.110.6822

Share and Cite

MDPI and ACS Style

Santos, J.M.; Vetere, A.; Wisniewski, A., Jr.; Eberlin, M.N.; Schrader, W. Comparing Crude Oils with Different API Gravities on a Molecular Level Using Mass Spectrometric Analysis. Part 2: Resins and Asphaltenes. Energies 2018, 11, 2767. https://doi.org/10.3390/en11102767

AMA Style

Santos JM, Vetere A, Wisniewski A Jr., Eberlin MN, Schrader W. Comparing Crude Oils with Different API Gravities on a Molecular Level Using Mass Spectrometric Analysis. Part 2: Resins and Asphaltenes. Energies. 2018; 11(10):2767. https://doi.org/10.3390/en11102767

Chicago/Turabian Style

Santos, Jandyson M., Alessandro Vetere, Alberto Wisniewski, Jr., Marcos N. Eberlin, and Wolfgang Schrader. 2018. "Comparing Crude Oils with Different API Gravities on a Molecular Level Using Mass Spectrometric Analysis. Part 2: Resins and Asphaltenes" Energies 11, no. 10: 2767. https://doi.org/10.3390/en11102767

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop