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Apparent disaggregation of colloids in a magnetically treated crude oil

PREPRINT of the paper published in: Energy & Fuels, V.23, Iss.8, pp.4016-4020 (2009). Apparent Disaggregation of Colloids in a Magnetically Treated Crude Oil
Igor N. Evdokimov,* and Konstantin A. Kornishin Department of Physics, Gubkin Russian State University of Oil and Gas, Leninsky Prospekt, 65, Moscow B-296, GSP-1, 119991, Russia Abstract.
“The new physical mechanism” of viscosity reduction of petroleum fluids was suggested in a series of recent publications. The key idea is that magnetic field treatment aggregates colloidal particles inside a crude oil into larger ones, thus decreasing viscosity. On the basis of new experimental data and of the analysis of well-proven theoretical models, we conclude that this “physical mechanism” in magnetically treated oils appears to be non-existent. In particular, as revealed by our optical measurements, magnetic treatment results in disaggregation of ________________________________________________________ * To whom correspondence should be addressed. E-mail: Introduction
Over the past years it has been repeatedly claimed that magnetic/electric field treatment may have beneficial effects on the properties of crude oils. The most frequently reported were cases of significant viscosity improvement. Recently, “the new physical mechanism” of viscosity reduction was suggested in a series of papers in Energy & Fuels and in other publications.1-7 The key idea is that magnetic (or electric) field treatment aggregates asphaltene (or paraffin) particles inside crude oil into larger ones. In turn, particle aggregation is the cause of the observed viscosity decrease. The authors claim that this basic mechanism of viscosity is universal and powerful for all liquid suspensions with broad applications, present ones and future ones. They also claim that laboratory tests confirm their theory. It appears, however, that some of the above statements and conclusions are not justified and are at odds with established knowledge. The discussed publications give the impression that the authors may not be familiar with well-known data on asphaltene aggregation effects on petroleum rheology. In fact, there is multiple and conclusive evidence that aggregation of asphaltenes (at constant concentration) increases the viscosity of petroleum. E. g., it is well- proven, that when asphaltene particles in the stored (degrading) oil become prone to aggregation, the viscosity of oil increases.8 Back in 1932, Mack9 measured viscosity of Mexican asphalts and suggested that the significant viscosity increase is due to strong aggregation of asphaltene particles. In a number of publications it has been concluded that association of asphaltene particles in crude oil and in vacuum residue can be distinguished by a corresponding increase of viscosity.10-13 Storm and Sheu14 applied four viscosity models for a colloidal dispersion to experimental data on viscosity of a vacuum residue and concluded that high viscosity was due to increase of volume of asphaltene particles. Fenistein et al.15 have shown that viscosity variations paralleled those of the volume of asphaltene aggregates as determined from the neutron scattering data. More recent experimental results of Luo and Gu16 again demonstrated that if the dispersed asphaltene particles aggregate and become large enough, the heavy oil viscosity increases significantly. Finally, Johansson et al.17 reported experimental decrease of viscosity in asphaltene solutions and attributed it to disintegration of oligomeric aggregates into monomers. They also noted that enhanced asphaltene association increased the viscosity of the solution. It is true, however, that there are insufficient experimental data on long-term changes in the state of aggregation after magnetic treatment of crude oils, though viscosity reduction has been observed by many authors.18-27 Some indirect evidence of post-treatment disaggregation was obtained by microscopy of deposits19-21 and by measuring the number of inhibition (paramagnetic, etc.) centres.25,27 The direct detailed experiments have demonstrated only temporary orientation of some petroleum constituents under the action of an applied magnetic field.28-30 In the present paper we describe experimental studies of a magnetically treated crude oil by optical methods which have been shown to be sensitive to the state of asphaltene aggregation.31-33 Experimental Section
Crude Oil. The studied virgin crude oil was collected directly from an oil-producing well
at Aznakayevsky reservoir in Tatarstan, Russia. After water separation, this oil had a specific gravity (SG) of 0.8756, contained 3.6 wt. % asphaltenes, 1.8 wt. % sulfur, ~6 wt. % paraffins/waxes. Previously, it has been repeatedly demonstrated that crude oils from this origin decrease their viscosity after treatment of flowing oils by constant magnetic fields.34, 35 Magnetic Treatment. The experimental set-up was based on a permanent C-shaped
magnet with a high-homogeneity field in the 12 mm gap between parallel circular poles. The magnetic field strength was 0.12 T as measured by proton resonance meter. In each of eleven experiments, we employed four 2 ml oil samples in sealed glass tubes inclined by ca. 20o to the horizontal plane. After filling the tubes, the samples were allowed to equilibrate for 30 minutes. One pair of samples was placed into the pole gap of the magnet; another pair remained outside magnetic field. In each pair, one sample remained stationary; the other was rotated with a frequency of 55-60 revolutions per minute (cf. the scheme of experimental setup in Figure 1). This oil treatment procedure continued for 1 hour at 20-23 oC; afterwards optical properties of all samples were measured within 2-3 minutes. Figure 1. Experimental setup for magnetic treatment of the crude oil (for details – cf. text).
Measurements of Optical Properties. The refractive index (RI) measurements were
performed in an Abbe-type refractometer IRF-454-B2M (KOMZ, Kazan, Russia).33 For toluene at 20 oC the measured RI was 1.4967, close to the value of 1.4969 quoted by the producer. The UV-visible extinction (UVVE) spectra in the 205-535 nm range have been measured with a Shimadzu UV-2201 UV/VIS double-beam recording spectrophotometer.32 The UVVE data were collected with 1 nm wavelength increment and automatically stored. The obtained data sets were computer-processed according to the below described procedures. Extension of UVVE measurements to larger wavelengths (310-750 nm range) was obtained by studying toluene solutions of oils in a spectrometer, equipped with a set of narrow-band light filters (KFK-2 Photocolorimeter).31 All optical measurements were performed at 20 oC and at ambient pressure. Results and Discussion
Experimental evidence of disaggregation in magnetically treated oil. Table 1 shows
mean values and standard deviations for RI in four types of oil samples employed in our experiments. In agreement with previously reported studies,18-27 a statistically significant effect was achieved only in case of magnetic treatment of a flowing (agitated) crude oil. Namely, a decrease of RI by ca. 0.2% was registered in samples rotated in a magnetic field. Table 1. Results of refractive index measurements in magnetically treated and control samples of
a crude oil. Values of specific gravity and of molecular weight are estimated by empirical 1.5380±0.0006 1.5405±0.0007 1.5404±0.0004 1.5403±0.0007 0.8706±0.0012 0.8759±0.0014 0.8756±0.0008 0.8755±0.0014 Multiple experimental studies have proved a strong correlation of RI with a specific gravity (density, API gravity) and an average molecular weight (AMW) of native crude oils,36-39 which, in turn, are correlated with oil viscosities.40 Accordingly, two bottom lines of Table 1 show the respective values of specific gravity and AMW estimated from experimental RI data by using empirical correlations from Refs. 37,38. There is an apparent decrease of both SG and AMW by ∼0.6% and ∼1% by in samples rotated in a magnetic field. The theoretical expression of RI-density relationship showing closest agreement with experiment is the formula of Lorentz and Lorenz:41 where KL is the specific refractivity in terms of the refractive index, n and the density ρ. The specific refractivity has been shown to be substantially independent of the state of aggregation and relatively invariant to change in temperature.36,41,42 Hence, at a constant temperature, the
observed lower RI values in magnetically treated samples may be reliably attributed to well- known density (specific gravity) decrease in fluids via bond break-up and deaggregation,43,44 Computer simulations have shown that these processes should be accompanied by a decrease of fluid’s viscosity.44 An exception is a case where colloidal particles are stabilised by strongly absorbed solvent molecules. In such system structure-breaking in colloidal aggregates is counteracted by structure-building at the increased interface area; hence the net effect is an increase of bulk density.45-47 The data of Table 1 suggest that such stabilization/absorption effects are negligible in a colloidal system of the studied crude oil. Additional proof of disaggregation in magnetically treated oil was provided by measurements of optical extinction. Figure 2 shows Shimadzu UV-2201 extinction spectra of non-treated oil (1) and of a crude oil sample rotated in a magnetic field (2); note a log scale for extinction. Clearly seen is a decrease of extinction after magnetic treatment at all wavelengths. The details of this effect were emphasized by computing the ratio of extinction in a treated sample to extinction in the original crude oil, as illustrated in Figure 3. Solid line – the data from Figure 2; open circles connected by dashed line – the data from KFK-2 Photocolorimeter. Figure 2. Optical extinction spectra of the original (1) and of magnetically treated (2) crude oil.
Optical extinction of crude oils is conventionally discussed48,49 within the Rayleigh limit when extinction cross-section is considered to be a sum of the absorbance and scattering contribution, σext = σabs + σscatt. Aggregation effects on absorbance were shown to be negligible at asphaltene concentrations characteristic to non-diluted crude oils,31,32 while the Rayleigh scattering cross-section is extremely sensitive to any changes in the radii r of colloidal 2 π ⎛ n −1 ⎞
n + 2
where λ is the wavelength of the incident light and n is the ratio of the particle RI to the RI of continuous phase.49 Accordingly, the overall decrease of extinction may be regarded as a qualitative proof of magnetic field - induced decrease of the size of suspended colloidal particles. It should be noted, however, that the relative decrease of Rayleigh scattering is expected to be independent on the incident wavelength, while Figure 3 shows a step-like change from a value of ∼0.875 below 300 nm, to another fairly constant level of ∼0.95-0.96 above ca. 370 nm. A plausible interpretation may be a different degree of magnetic action on smaller and larger crude oil molecules. The most effective absorbers below 300 nm are known to be low molecular weight species with 1-2 ring aromatic chromophores, while absorbance in the visible and in the near-IR ranges is due to the presence of heavier asphaltene molecules with multiple-ring aromatic Figure 3. Relative decrease of crude oil’s optical extinction after magnetic treatment.
The appearance of two local minima in the longer-wavelengths part of Figure 3 may be regarded as an additional support of the above interpretation as these are indicative of relatively stronger magnetic field effects on the specific molecular species. In particular, the position of these minima coincide with positions of the strong Soret and the weaker Qα and Qβ absorption bands in vanadyl porphyrins51 (at 410, 553 and 573 nm as indicated by vertical lines in Figure 3). Furthermore, it has been experimentally demonstrated that vanadyl porphyrins are accumulated only in asphaltene sub-fractions with the lowest molecular weights.
Theoretical models do not support “the new physical mechanism” of viscosity
reduction via particle aggregation. As discussed in Introduction, the authors of Refs.1-7 claim
that this “basic mechanism of viscosity” is universal and powerful for all liquid suspensions. However, their theory of this mechanism obviously is the result of false assumptions and serious misinterpretations. In particular, consider the following statement from Ref. 2 on relation of viscosity η to the particle size at constant volume fraction φ: “While a profound theory for this size effect is still lacking, the following qualitative explanation helps our understanding. Generally, the effective viscosity depends on how much freedom the suspended particles have in the suspension. The less freedom for the particles, the faster the energy dissipates and the higher the effective viscosity. The mean free path of the spheres inside the suspension is given by la/(3φ), where a is the particle radius. As a gets bigger, l becomes longer, indicating that the suspended particles have more freedom to move in the suspension. Thus, η goes down.” This qualitative conclusion of increasing l with increasing a may have followed only from an over-simplified elementary kinetic theory of ideal gases54 with an additional restricting assumption that primary suspended particles do not flocculate (retaining their identities) into irregular-shaped aggregates but coalesce into new spherical species. Under these assumptions, l∼1/na2 where n is the number density of particles. At constant φ, n∼1/a3; hence it may be In fact, realistic theories of disordered media, free from simplifying assumptions, show that the larger are the diffusing particles, the smaller is the mean free path at constant volume Another argument for the new “basic mechanism of viscosity” concerns the behaviour of a maximum volume fraction, φm, an important “crowding” parameter in a number of models, e.g. in the Krieger-Dougherty’s formula for effective viscosity of a liquid suspension:57 where η0 is the viscosity of a base liquid and [η] is a so-called intrinsic viscosity (equal to 2.5 for In Ref.1 the authors of “the new mechanism of viscosity” insist that magnetic field “aggregates the small particles into large ones. … While this change in rheology does not alter φ, it makes φm increased as a result of the increase of … average particle size. Hence, the effective viscosity η is reduced.” As above, this conclusion obviously comes from misunderstanding of aggregation phenomena in solid suspensions. An increase of φm with increasing size is possible only in very rare cases (e.g. in emulsions) where new compact particles (aggregates) are formed by total coalescence of smaller ones.58,59 In solid suspensions, however, aggregation always proceeds via flocculation of smaller particles into non-compact clusters (open structures containing entrapped Since Mooney,60 φm is interpreted as the volume fraction at which particles (aggregates) fill the available space and the viscosity increases because of mechanical interlocking. For rigid individual spheres, independent of size, the maximum φm=0.74 is achieved in hexagonal close packed arrays. However in suspensions of flocculated open clusters space-filling commences at much lower concentrations of primary particles, i.e. φm decreases (and effective viscosity increases) with increasing size. The magnitude of these effects depends on the volume fraction of int 0.74, as illustrated in Figure 4. Solid curves are theoretical evaluations of relative viscosity ηrel=η/η0 which have shown a good agreement with Figure 4. Increase of relative viscosity as a result of particle aggregation in a suspension. Curve
1: primary particles do not form aggregates; curve 2: φint=0.65 (cubic centered packing of particles inside aggregates); curve 3: φint=0.56 (simple cubic packing of particles inside Summarizing, the crucial theoretical arguments in Refs. 1-7 supporting the ”basic mechanism of viscosity” are not justified and are at odds with well-established knowledge in rheology of aggregating suspensions. Characteristically, some of these publications recently were also criticized for claims and conclusions that violate the first law of thermodynamics.62 Possible molecular mechanisms of magnetic treatment. After this paper was submitted
for publication, one of the reviewers requested more discussion for particular chemical (molecular) mechanisms of magnetic treatment effects in crude oils. Regretfully, literature analysis shows that at the moment this subject is still under-investigated, hence any suggested model would be merely speculative. Various mechanisms of magnetic action have been proposed, but not proven conclusively. E.g., some groups of scientists ascribe a key role to charged species in petroleum and to arising Lorentz forces which can destroy molecular aggregates.19 Other authors discuss the magnetic treatment effects in terms of intrinsic magnetic properties of asphaltene colloids.18,27 Presumably, asphaltene particles may be either ferromagnetic (due to ferrous micro-contaminants),63 paramagnetic27,64 or diamagnetic.65 However, the implicit controversy in models with magnetic asphaltenes is that such particles may be expected not to disaggregate, but to flocculate under the action of a magnetic field.66 Some other molecular mechanisms are discussed in publications on specially formulated electrorheological and magnetorheological fluids,67-69 in particular, external field effects on hydrogen bonding.69 In our previous publication we have discussed the importance of easily disrupted hydrogen bonds in asphaltene aggregates.70 Hence, a plausible cause of the above discussed disaggregation of petroleum colloids may be a transient break-up of hydrogen bonds between asphaltene molecules. Conclusions
Recent suggestion of “the new physical mechanism” of viscosity reduction via particle aggregation has added unnecessary confusion to a still controversial topic of magnetic field effects in crude oils. On the basis of the above experimental and theoretical evidence, we may conclude that this “physical mechanism” in magnetically treated oils appears to be non-existent. The widespread circulation of scientifically untenable "explanations" does little to inspire confidence in any beneficial effects of magnetic treatment of petroleum. However, unbiased experiments increasingly report evidence that magnetic treatment may significantly alter the colloidal properties of asphaltenes and paraffins in crude oils. Further research is needed to reveal the true molecular nature of these effects. Acknowledgements
The authors are indebted to Mr. I. V. Kovalenko and Mr. A. P. Losev for their assistance References
(1) Tao, R.; Huang, K.; Tang, H.; Bell, D. Electrorheology leads to efficient combustion. Energy Fuels 2008, 22, 3785-3788.
(2) Tao, R.; Xu, X. Reducing the Viscosity of Crude Oil by Pulsed Electric or Magnetic Field. Energy Fuels 2006, 20, 2046-2051.
(3) Tao, R. The Physical Mechanism to Reduce Viscosity of Liquid Suspensions. Int. J. Mod. Phys. B 2007, 21, 4767–4773.
(4) Tao, R.; Huang, K.; Tang, H.; Bell, D. Electrorheology leads to efficient combustion. Abstract B15.00010 at the March Meeting of The American Physical Society, Pittsburgh, Pennsylvania, (5) Tao, R. The Physical Mechanism to Reduce Viscosity of Liquid Suspensions. In Electrorheological Fluids and Magnetorheological Suspensions (ERMR 2006); Gordaninejad, F., Graeva, O.A, Fuchs, A., D. York, D., Eds.; World Scientific: New Jersey, USA, 2007; p. 21-28. (6) Tao, R.; Xu, X. Viscosity Reduction in Liquid Suspensions by Electric or Magnetic Fields. In Electrorheological Fluids and Magnetorheological Suspensions (ERMR 2004); Lu, K., Shen, R., Hou, M., Eds.; World Scientific: New Jersey, USA, 2005; p. 299-305. (7) Tao, R.; Xu, X. Method for Reduction of Crude Oil Viscosity. European Patent Application (8) Speight, J. G. Petroleum Chemistry and Refining. CRC Press: New York, 1997. (9) Mack, C. Colloid chemistry of asphalts. J. Phys. Chem. 1932, 36, 2901–2814.
(10) Storm, D. A.; Barresi, R. J.; DeCanio, S. J. Colloidal nature of vacuum residue. Fuel 1991,
(11) Escobedo, J.; Mansoori, G. A. Viscometric determination of the onset of asphaltene flocculation: a novel method. SPE Prod. Facil. 1995, May, 115–118. (12) Escobedo, J.; Mansoori, G. A. Theory of Viscosity as a Criterion for Determination of Onset of Asphaltene Flocculation. SPE paper 28729, 1996. (13) Rao, B. M. L; Serrano, J. E. Viscometric Sudy of Aggregation Interactions in Heavy Oil. Pet. Sci. Technol. 1986, 4, 483-500
(14) Storm, D. A.; Sheu, E. Y. Rheological studies of Ratawi vacuum residue at 366 K. Fuel 1993, 72, 233–237.
(15) Fenistein, D.; Barre, L.; Broseta, D.; Espinat, D.; Livet, A.; Roux, J. N.; Scarsella, M. Viscosimetric and Neutron Scattering Study of Asphaltene Aggregates in Mixed Toluene/Heptane Solvents. Langmuir 1998, 14, 1013-1020.
(16) Luo, P.; Gu, Y. Effects of asphaltene content on the heavy oil viscosity at different temperatures. Fuel 2007, 86, 1069–1078.
(17) Johansson, B.; Friman, R.; Hakanpää-Laitinen, H.; Rosenholm, J. B. Solubility and interaction parameters as references for solution properties II Precipitation and aggregation of asphaltene in organic solvents. Adv. Colloid Interf. Sci. 2009, 147–148, 132–143.
(18) Morozov, V. I.; Usatenko, S. T.; Savchuk, O. V. Influence of a magnetic field on the physical properties of hydrocarbon fluids. Chem. Tech. Fuels Oils 1977, 13, 743-746.
(19) Marques, L. C. C.; Rocha, N. O.; Machado, A. L. C.; Neves, G. B. M.; Vieira, L. C.; Dittz, C. H. Study of Paraffin Crystallization Process Under The Influence of Magnetic Fields and Chemicals. Paper SPE 38990, Fifth Latin American and Caribbean Petroleum Engineering Conference and Exhibition, Rio de Janeiro, Brazil, 1997. (20) Rocha, N.; Gonzalez, G.; do C. Marques, L. C.; Vaitsman, D. S. A Preliminary Study on the Magnetic Treatment of Fluids. Pet. Sci. Technol. 2000, 18, 33-50.
(21) Tung, N. P.; Vinh, N. Q.; Phong, N. T. P.; Long, B. Q. K.; and Hung, P. V. Perspective for using Nd–Fe–B magnets as a tool for the improvement of the production and transportation of Vietnamese crude oil with high paraffin content. Physica B 2003, 327, 443-447.
(22) Loskutova, Y. V.; Yudina, N. V. Effect of Constant Magnetic Field on the Rheological Properties of High-Paraffinicity Oils. Colloid J. 2003, 65, 469-474.
(23) Tung, N. P.; Vinh, N. Q. Rheological improvement for paraffin crude oil flows treated by Nd-Fe-B magnetic fields in non-Newtonian fluid area. In Proceedings of the Ninth Asia Pacific Physics Conference (9th APPC), Hanoi, Vietnam, 2004. (24) Loskutova, Y. V.; Prozorova, I. V.; Yudina, N. V.; Rikkonen, S. V.; Daneker, V. A. Change in the Rheological Properties of High-Paraffin Petroleums under the Action of Vibrojet Magnetic Activation. J. Eng. Phys. Thermophys. 2004, 77, 1034-1039.
(25) Loskutova, Y. V.; Yudina, N. V. Rheological behavior of oils in a magnetic field. J. Eng. Phys. Thermophys. 2006, 79, 105-113.
(26) Salavatov, T. S. Application of Physical Fields for Increasing Oil Recovery Efficiency. Energ. Source A 2006, 28, 365–372.
(27) Loskutova, Y. V.; Yudina, N. V.; Pisareva, S. I. Effect of magnetic field on the paramagnetic, antioxidant, and viscosity characteristics of some crude oils. Petrol. Chem. 2008, 48, 51-55.
(28) Shao, H. H.; Gang, H.; Sirota, E. B. Magnetic-field induced orientation and anisotropic susceptibility of normal alkanes. Phys. Rev. E 1998, 57, R6265–R6268.
(29) Kimura, T.; Yamato, M.; Koshimizu, W.; Kawai, T. Magnetic-field Induced Orientation of Paraffin. Chem. Lett. 1999, 28, 1057-1058.
(30) Kaneko, Y.; Onodera, T.; Kasai, H.; Okada, S.; Oikawa, H.; Nakanishi, H.; Fukuda, T.; Matsuda, H. Reversible and efficient anisotropic orientation of dispersed aromatic hydrocarbon nanocrystals in a magnetic field. J. Mater. Chem. 2005, 15, 253-255.
(31) Evdokimov, I. N.; Eliseev, N. Yu.; Akhmetov, B. R. Assembly of asphaltene molecular aggregates as studied by near-UV/visible spectroscopy. II. Concentration dependencies of absorptivities. J. Petr. Sci. Eng. 2003, 37, 145-152.
(32) Evdokimov, I. N.; Losev, A. P. On the Nature of UV/Vis Absorption Spectra of Asphaltenes. Pet. Sci. Technol. 2007, 25, 55-66.
(33) Evdokimov, I. N.; Losev, A. P. Effects of molecular de-aggregation on refractive indices of petroleum-based fluids. Fuel 2007, 86, 2439-2445.
(34) Chernova K. V. Developments and prospects in application of magnetic treatment to produced crude oils. Monographia Publ.: Ufa, 2005. [In Russian] (35) Loskutova, Yu. V. Effect of a magnetic field on the rheological properties of crude oils. Cand. Sci. Thesis, Inst. Petrol. Chem. RAS: Tomsk, 2004. [In Russian] (36) Harrison, D. V.; Reingold, A. M.; Turner, W. R. Volume Changes in Petroleum Waxes as Determined from Refractive Index Measurements. J. Chem. Eng. Data 1958, 3, 352–359.
(37) Buckley, J. S.; Wang, J. Crude oil and asphaltene characterization for prediction of wetting alteration. J. Petr. Sci. Eng. 2002, 33, 195-202.
(38) Buckley, J. S.; Morrow, N. R.; Fan, T.; Wang, J.; Yang, L.; Bays, S. Wettability and imbibition: microscopic distribution of wetting and its consequences at the core and field scales. Semiannual Report (DE-AC26-99BC15204). PRRC, New Mexico Institute of Mining and (39) Bayat, M.; Sattarin, M.; Teymouri, M. Prediction of Asphaltene Self-Precipitation in Dead Crude Oil. Energy Fuels 2008, 22, 583–586.
(40) Sattarin, M.; Modarresi, H.; Bayat, M.; Teymori, M. New Viscosity Correlations for Dead Crude Oils. Petroleum & Coal 2007, 49, 33-39.
(41) Jaffe, H. W. Crystal Chemistry and Refractivity. Courier Dover Publ.: New York, 1996. (42) Rietveld, B. J. Application of specific refractive index increments for determination of partial specific volumes of dissolved macromolecules. J. Polym. Sci. Pol. Phys. 1972, 8, 1837-
(43) Aliotta, F.; Ponterio, R. C.; Saija, F. On the Origin of Excess Thermodynamic Quantities in Liquid Mixtures. Oil Gas Sci. Technol. 2008, 63, 353-361.
(44) Wensink, E. J. W.; Hoffmann, A. C.; van Maaren, P. J.; van der Spoel, D. Dynamic properties of water-alcohol mixtures studied by computer simulation. J. Chem. Phys. 2003, 119,
(45) Regdon, I.; Dekany, I. Nanolayer liquid density on hydrophobic surfaces. Colloid Polym. Sci. 1998, 276, 1145-1150.
(46) Papp, S.; Dékány, I. Structural properties of palladium nanoparticles embedded in inverse microemulsions. Colloid Polym. Sci. 2001, 279, 449-458.
(47) Everett, D. H. Reporting data on adsorption from solution at the solid/solution interface. Pure Appl. Chem. 1986, 58, 967-984.
(48) Joshi, N. B.; Mullins, O. C.; Jamaluddin, A.; Creek, J.; Jim McFadden, J. Asphaltene Precipitation from Live Crude Oil. Energy Fuels, 2001, 15, 979–986.
(49) Aske, N.; Kallevik, H.; Johnsen, E. E.; Sjöblom, J. Asphaltene Aggregation from Crude Oils and Model Systems Studied by High-Pressure NIR Spectroscopy. Energy Fuels 2002, 16, 1287-
(50) Mullins, O. C. Optical Interrogation of Aromatic Moieties in Crude Oils and Asphaltenes. In: Structures and Dynamics of Asphaltenes, O. C. Mullins and E. Y. Sheu, Eds., Springer: New (51) Doukkali, A.; Saoiabi, A.; Zrineh, A.; Hamad, M.; Ferhat, M.; Barbe, J. M.; Guilard, R. Separation and identification of petroporphyrins extracted from the oil shales of Tarfaya: geochemical study. Fuel 2001, 81, 467-472.
(52) Yokota, T.; Scriven, F.; Montgomery, D. S.; Strausz, O. P. Absorption and emission spectra of Athabasca asphaltene in the visible and near ultraviolet regions. Fuel 1986, 65, 1142-1149.
(53) Marques, J.; Merdrignac, I.; Baudot, A.; Barre, L.; Guillaume, D.; Espinat, D.; Brunet, S. Asphaltenes Size Polydispersity Reduction by Nano- and Ultrafiltration Separation Methods – Comparison with the Flocculation Method. Oil Gas Sci. Technol. 2008, 63, 139-149.
(54) Warren, W. S. The physical basis of chemistry, 2d ed., Academic Press: New York, 2000. (55) Lu, B.; Torquato, S. Chord-length and free-path distribution functions for many-body systems. J. Chem. Phys. 1993, 98, 6472- 6482.
(56) Cate, A. T.; Derksen, J. J.; Portela, L. M.; van den Akker, H. E. A. Fully resolved simulations of colliding monodisperse spheres in forced isotropic turbulence. J. Fluid Mech. 2004,
(57) Krieger, I. M.; Dougherty, T. J. A mechanism for non-Newtonian flow in suspensions of rigid spheres. Trans. Soc. Rheol. 1959, 3, 137-152.
(58) Mittal, K. L.; Kumar, P. Handbook of Microemulsion Science and Technology. CRC Press: (59) Goodwin, J. W.; Roy W. Hughes, R.W. Rheology for chemists: an introduction. Royal (60) Mooney, M. The viscosity of a concentrated suspension of spherical particles. J. Colloid Sci.
1951, 6, 162-170.
(61) Starov, V.; Zhdanov, V.; Meireles, M.; Molle, C. Viscosity of concentrated suspensions: influence of cluster formation. Adv. Colloid Interf. Sci. 2002, 96, 279-293.
(62) Gulder, O. L. Comments on “Electrorheology Leads to Efficient Combustion” by Tao et al. Energy Fuels, 2009, 23, 591–592.
(63) Shaidacov V. V.; Laptev A. B.; Golubev M. V. Magnetic Apparatuses in Oil and Gas Recovery. Electronic scientific journal "Oil and Gas Business", Ufa, 2003, 6p. [] (64) Semple, K. M.; Cyr, N.; Fedorak, P. M.; Westlake, D. W. S. Characterization of asphaltenes from Cold Lake heavy oil: variations in chemical structure and composition with molecular size.
Can. J. Chem. 1990, 68, 1092-1099.
(65) El-Mohamed, S.; Achard, M.-F.; Hardouin, F.; Gasparoux, H. Correlations between diamagnetic properties and structural characters of asphaltenes and other heavy petroleum products. Fuel 1986, 65, 1501-1504.
(66) Tsouris, C.; Scott, T. C. Flocculation of Paramagnetic Particles in a Magnetic Field. J. Colloid Interface Sci. 1995, 171, 319-330.
(67) Jordan, T. C.; Shaw, M. T. Electrorheology. IEEE T. Electr. Insul. 1989, 24, 849-878.
(68) Edamura, K.; Otsubo. Y. Electrorheology of dielectric liquids. Rheol. Acta 2004, 43, 180-
(69) Wen, W.; Huang, X.; Sheng, P. Electrorheological fluids: structures and mechanisms. Soft Matter 2008, 4, 200–210.
(70) Evdokimov, I. N.; Eliseev, N. Yu. Thermally Responsive Properties of Asphaltene Dispersions. Energy Fuels 2006, 20, 682-687.


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