Printer Friendly

Electrodeposicion de vanadio y niquel de los asfaltenos de crudos pesados: Ingenieria quimica.

V and Ni electrochemical deposition from asphaltenes in heavy oils

1. Introduction

Light Oil reserves are depleting and needs for transportation fuel liquids poses new problems to Refineries in order to meet the growing demand. Research and development in heavy oils has dramatically raised in last years (Campetrol, 2009) specially focus on resin-asphaltene concentrates (CRA). In Colombia 40 % of the proven reserves corresponds to heavy oils, present in 6 of 16 basins. For example one of these basins Llanos Orientales, counts on 6,806 MMbbl to 319,455 MMbbl probable reserves and actually participate with 73.5 % of the total oil production (Colombia y energia, 2013). Refining the heavy oils in the near future will help to solve production of fuel liquids for transportation.

Nature and structure of both resins and asphaltenes strongly depend on the origin of the oil (Nomura et al., 2005). Heavy oil from same reservoirs can show different properties (Tharanivasan, 2012). ASTM D6560-12, ASTM D3279 and ASTM D4124 are the most used methods for separation and characterization of asphaltenes and resins. Usually research laboratories use the precipitation of these components with aliphatic solvents and extraction with toluene in a Soxhlet reflux system, allowing a good separation of resins from asphaltenes (Aske, 2002). Citations on different models of the asphaltene structure are found, being one of them a model that considers a pillared layers of aromatic structures array (Leyva et al., 2013).

Resins and asphaltenes content in a concentrate type CRA generate industrial and environmental issues because they are highly viscous, high sulfur content, and contains more than 28 metals in form of traces of Pb, V, Ni, Cr, TI, Fe and Al (Welter et al., 2009), being nickel and vanadium in the porphyrin forms the most important in the heavy cuts. Metal concentration depends on origin of oil. Some authors reports vanadium content 1.0x[10.sup.-7] Kg/L to 1.2x[10.sup.-3] Kg/L, and for Ni 1.5x[10.sup.-4] Kg/L (Ali & Abbas, 2006); Colombian Castilla oil was reported having metal content in asphaltenes 1,686 and 431 [micro] g/g for V y Ni, (Mogollon, 1997).

Demetallization by electrolysis is a new route that might be used at moderated conditions of temperature in an convenient mix of solvents in a electrolytic solution. An efficiency of 85% is reported in a process of demetallization (Duyck et al., 2006) giving an opportunity to add value extracting the metals present in a heavy oil.

Vanadium and nickel that deactivate hydrocracking catalyst are present in two forms: heterocyclic porphyrins reported by Treibs A. (1936), and in non - porphyrin form with undefined structure (Khuhawaret et al., 2012). Porphyrinsareclassified as: etioporphyirines (Etio-), deoxofiloeritroetioporphyrin (DPED) observed by Barwise y Roberts (Fish & Wines, 1984) and later cited by Baker and Louda (1988), who discovered tetrahydrobenzoporphyrins, benzo-(rhodo)-etio-, and benzo-(rhodo)porphyrin. Ni in heavy oil is present in form of etioporphyrins (etio III) and are less investigated due to its low concentration compared with Vanadium that is present in form of vanadyl ion (-VO[2.sup.+]), axe coordinated to an oxygen and four Nitrogen atoms in structures type vanadyl-deoxofiloeritroetioporphyrin (VODPEP) and in vanadylbenzotioporphyrins (VOB) (Yin et al., 2006) as showed in Figure 1.

Commercial demetallization processes are at high pressures (1500-2500 psi) and temperature (380-450 [degrees]C), as demetallization process (Mello et al., 2012) in presence of Hydrogen that reacts with organometallics in the organic matrix (including metallporphyrins). Al laboratory level the most common method for determination of V and Ni is the acid digestion with strong organic acids at high temperature generating corrosive vapors.

Clean alternatives of demetallization are electrochemical processes as the one proposed by Welter et al. (2009), porphyrines present in asphaltenes, according to this work, ease the demetallization because they are electroactive and redox reactions occur under mild conditions of pressure and temperature. It was reported that metal elimination from a Venezuelan heavy crude oil Ayacucho resulted in a 84% extraction of Vanadium (IV) meso-tetra-phenolporphyrin and

78% V (IV) octa-etioporphyrin (VOHDM-OEP) using commercial porphyrins by electrochemical techniques. With oil porphyrins extractions rates were 66.4% and 64.1% using graphite electrode during 90 minutes and Pt electrode for 120 minutes. (Campero & Espinosa, 1996). The factors that affect this method: electrolytic solution, electrode material, time of reaction and reduction potential.

In this research the electrodeposition was carried out in two solutions evaluating the effect of electrochemical variables by voltammetric determination in the extraction of V and Ni from Castilla heavy crude oil on different electrode materials.

2. Methodology

2.1 Characterization of CRA and asphaltene probes.

CRA and asphaltenes probes obtained from Castilla crude oil were precipitated with nheptane and characterized by means of AE, FTIR techniques and atomic absorption (AAS).

2.1.1Elemental analysis

Content of carbon, hydrogen, sulfur and nitrogen was determined using 2 mg grinded probe in a FLASHEA 1112 series Analizator, Thermo ELECTRON CORPORATION at a temperature of 1000[grado]C.

2.1.2 Infrared Spectroscopy with Fourier Transform (FT-IR).

A spectrometer SHIMADZU IR-Affinity 1 was used for this analysis. It was determined the presence of functional groups and vibration bands assigned to asphaltenes, and also the anion V = O band at 1030 [cm.sup.-1], that is clear signal of the presence of metals in asphaltenes.

2.1.3. Quantification of V and Ni in Castilla CRA and asphaltenes. Acid wet digestion for metal extraction.

Probes of CRA and asphaltenes weight 3.0 [+ or -] 0.0001 g were calcined at a temperature 525 [degrees]C during 6 hours to eliminate organic material. Digestion procedure is a modification of ASTM D5863 Standard. Digestion was carried out taking an acid mix HNO 3/HCl (2:5). Tubes were sealed and a digest plate type HACH DRB 200 was used. Conditions of wet acid digestion were: temperature = 100 [degrees]C for 2 hours followed by hot filtration and weighed with distilled water. Quantification of metals was done in a Spectrometer Perkin Elmer 100, at working conditions shown in Table 1.

2.2 Electrochemical cell

An electrochemical cell was designed for experiments previous to electrolysis. A second cell with three compartments as seen in figure 2 with a volume probe capacity of 250 ml and a heating jacket with thermostat was built. Working electrode was a graphite bar with a O content 5.1 % and Cl 0.37% (measured by dispersive x-ray spectroscopy, EDX). A SEM analysis was also taken as shown in figure 3. Conterelectrode was built with a Pt wire 0.25 mm thickness. A silver wire 2 cm length immersed in a 0.01 M LiCO and 0.01 M AgNO in CH 3CN solution was used as reference.

2.3 Extraction of V and Ni by electrodeposition

Experiments on a potentiostat Autolab M101 were done to evaluate the effect of electrochemical variables (potential screen, reaction time and electrode materials for the electrodeposition) in the two mentioned electrolytic solution by voltamperommetry.

2.4 Cyclic voltammetry electrolytic solution and Castilla crude oil.

Experiments were done at different scanning velocities from 0 to -2000 mV vs. Ag/[Ag.sup.+]. 5 g of each product were used for V and Ni electrodeposition. A solution with 90 ml Li Cl [O.sub.4], 0.2 M in THF in presence of a protonating agent (mix 70 ml THF and 20 ml C[H.sub.3] OH) was used. Electrodeposition was carried at conditions that were previously determined. All the experiments were at room temperature and the time of the reaction was 24 hours under agitation.

2.5. Chronoamperommetry of Castilla crude oil

To obtain the chronoamperommetry for Castilla crude oil 5g were added to a solution with 150 ml LiCl[O.sub.4] 0.2 M THF in solution in the presence of the protonating agent CH OH . Measurements were done with permanent agitation at a constant potential either -1.0 or -1.7 V. Purge was done every time with Nitrogen during 10 min.

3. Results

Concentrate content (CRA) in Castilla crude oil was determined as 23.21% .Also resin content 2.81 % and 20.04 [+ or -] 1.1 % asphaltenes were found, that is according with the classification of this crude oil as heavy oil having an API gravity of 9.6 , showing a high resin and asphaltene content.

From the element analysis and the H/C relation, empirical formula and average weight empirical formula (PFEA) were calculated for asphaltenes and CRA concentrate. Empirical formula were [C.sub.59] [H.sub.63] NSO and [C.sub.63] [H.sub.74] NSO for Castilla asphaltenes and CRA respectively. A less content of C and H in asphaltenes is found due to the resin elimination. The higher relation H/C determines a less aromatic character in asphaltenes as shown in Table 2.

FT-IR spectra for CRA and asphaltenes from Castilla (see figures 4 and 5) showed similarity at the bands in same frequencies. Each one gives absorption bands for aromatic structures at 3010 and 3235 ([v.sub.CH-Ar1]), 1599 and 1615 ([v.sub.C = 0] aromatic), 861 and 864 ([[gamma].sub.CH-Ar1]) or ring structures with H alone, 810-808 ([[gamma].sub.CH-Ar2, 3]) or ring with 2H nearby, 726 and 746 [cm.sup.-1] ([[gamma].sub.CH-Ar4]) or rings with 4H nearby and vibration bands assigned to aliphatic groups in 2922-2921 ([v.sub.CH3+CH2) and 1375,1455 [cm.sup.-1] ([[delta].sub.CH3+CH2]). Ether signal appears only for asphaltenes at 1029 cm-1 and carbonyl signal at 1637 cm-1 only for CRA. Both probes give bands associated to a N-H bond.

3.1. Results of content quantification for V and Ni in CRA and Asphaltenes by flame atomic absorption

Results for calibration curves for determining V and Ni content (absorbance [+ or -] 0.001) versus concentration is shown in figure 6. Using equation (1) that relates absorbance and metal concentration a content of 4.41x[10.sup.-4] Kg/L of V and 5.86x[10.sup.-5] Kg/L of Ni were found in Castilla crude oil probes. Similar results are reported by the Colombian Oil Institute (ICP): V y Ni content in Castilla crude oil are 1.85x[10.sup.-3] Kg/L y 3.82x[10.sup.-4] 4 Kg/L respectively (Campetrol, 2009).

[y] = m[x] + b


concentration = [x] = [Kg/L], absorbance = [y]= [dimensionless], tangent= [m] = [L/Kg],

intercept= [b]= [dimensionless]

3.2. Cyclic voltammetry (VC) electrolytic medium and Castilla crude oil.

Effect of electrolytic medium on the metal recuperation by electrochemical way by means of VC was studied. In the figure 7 voltamperogramms at 0 and 2,300 mV vs Ag/AgCl, are shown. Electrolytic medium on Pt does not show associated peaks with reactions on the catalyst in the interval of potential measurements. However, at more negative potential an increase in current densities it is observed, a fact that could be assigned to a medium decomposition as reported in a publication (Marquez et al., 2006).

On the graphite electrode surface as working electrode (figure 8), no peaks were observed in the voltamperommetric experiments. That indicates that the chosen potential interval is the adequate.

In figure 9a is shown the voltamperogramm of Castilla crude oil in acetonitrile, observing a reduction wave nearby to -1.0 V that could be assigned to the anion radical formation caused by the reduction of the [pi] system in the porphyrinic ring. In figure 9b peak of the radical anion formation appears at -1.2 V, displaced 0.2 V to less negatives potentials due probably to a solvent effect. In this case the effect of THF on the solubility of the petroporphyrins in the solvent (Yin C., 2008).

With the purpose to find the reaction time the probe stayed in contact with the working electrode for 15 hours, finding that the peak at -1.0 V (figure 10a) is less remarkable that the same peak but with the electrode at a contact time of 2 hours (figure 10b

The conclusion could be that the reaction occurs very slow and other electrochemical parameters must be studied in a more detailed way to diminish time reaction or find a right crude oil concentration to increase the product yield.

3.3. Chronoamperommetry Castilla crude oil

Chronoamperommetry Castilla crude is shown in figure 11. It can be observed a typical current characteristic, that it means than the species on the electrode surface are slowly diminishing with time. It is remarkable that under constant and mild agitation concentration on electrode active surface can reach a stationary value current. Respecting to V and Ni concentrations the molar relation mM of V:Ni was calculated and resulted in a value of 8:1. With this molar relation and the C charge obtained from the chronoamperommetry of Castilla crude the V and Ni mass deposited was calculated as 2,37x[10.sup.-5] g.

4. Conclusions

Concentration of V and Ni metals determined by atomic absorption in this work was greater in an order of magnitude than the concentrations reported by Colombian Oil Institute for the same probes of Castilla crude oil. (4.4x[10.sup.-4] Kg/L for V and 5.86x[10.sup.-5] Kg/L for Ni). With the experimental data obtained by cyclic voltammetry a potential threshold of 0 to -2,3000 V was determined. In this interval the medium does not present reduction peaks or collateral reactions that could affect

Castilla crude oil probe. Besides, it was possible to find the reaction time for the probe in contact with working electrode as 15 hours, finding the peak at -1.0 V. It was chosen the best graphite material with less impurities for the elaboration of the working electrode referred to SEM technique. Electrodeposition reaction is slow and is affected by electrochemical factors as reaction time and the yield of the process. The low deposition of the metals V and Ni by this electrochemical technique is probably due to the quantity of other metals present in crude oil that interfere, because they form different structures of organic and non organic compounds like Cl and S salts that are known to be in crude oil. Porphyrins containing V, Ni and Fe (III) or Fe (II) are very stable due to the high chelating properties and difficult to go through a reduction process.

5. Acknowledgement

Authors want to thank Vicerrectoria de investigaciones Universidad del Valle, for the financial support to the Project CI- 7902 "Determination of V and Ni of petroporphyrins by por electrodeposition". Also to the Chemist Jose Marquez who helped in the cell design.

6. References

Ali, MF., & Abbas, S. (2006). A review of methods for the demetallization of residual fuel oils. Fuel Process. Technol., 87 (7), 573-584

Aske, N. (2002). Characterisation of Crude Oil Components, Asphaltene Aggregation and Emulsion Stability by Means of Near Infrared Spectroscopy and Multivariate Analysis. Doctoral Thesis, Department of Chemical Engineering. Norwegian University of Science and Technology, Trondheim, Norwegian.

ASTM International.Annual Book of Standards ASTM D5863 (2011). Method A: Determination of nickel, vanadium, Fe and Na in crude oils and residual fuels by flame atomic absorption spectroscopy. USA. West Conshohocken, PA.

Campero, B. A., & Espinosa, M. (1996). Distribution of vanadylporphyrins in a Mexican off shore heavy crude oil. Fuel Process. Technol., 46 (3), 171-182

Campetrol (Camara Colombiana de servicios petroleros).(2009). La produccion de los distintos tipos de crudo en Colombia. Bogota .Colombia Colombia Energia, la revista de la industria energetica colombiana (2013). Crudos pesados un nuevo horizonte. http://www.colombiaenergia. com/ediciones

Duyck, C., Miekeley, N., Porto Da Silveira, C.L., Aucelio, R.Q., Campos, R.C., Grinberg, P., & Brandao, G.P. (2007). The determination of trace elements in crude oil and its heavy fractions by atomic spectrometry. Spectrochim. Acta. Part B. Spectrosc. 62 (9), 939-951.

Fish, R., Komelenic, & J., Wines, B. (1984). Characterization and comparison of vanadyl and nickel compounds in heavy crude petroleums and asphaltenes by reverse-phase and size-exclusion liquid chromatography/graphite furnace atomic absorption spectrometry. Anal. Chem. 56 (13), 2452-2460.

Khuhawar, M.; Mirza, M., & Jahangir, T. (2012). Determination of metal ions in crude oil. Intech., 65, 121-144.

Leyva, C., Ancheyta, J., Berrueco, C., & Millan, M. (2013). Chemical characterization of asphaltenes from various crude oils. Fuel Process. Technol., 106, 734-738.

Marquez, J., Perez de Marquez, O., Balladores, Y. (2006). Demetalizacion de petroporfirinas por via electroquimica directa. Tesis de doctorado, Departamento de Quimica, Universidad de los Andes, Merida, Venezuela.

Mello, P.A., Pereira, J.S., Mesko, M.F., Barin, J.S., & Flores, E.M. (2012). Sample Preparation Methods for Subsequent Determination of Metals and Non-Metals in Crude Oil. Anal. Chimica Acta, 746, 15-36.

Mogollon, L., Rodriguez, R., Larrota, W., Ortiz, C., & Torres, R., (1997). Fraccionamiento y desmetalizacion biocatalitica de asfaltenos de crudo Castilla. CT&F Ciencia tecnologia y futuro 1 (3), 109-121.

Nomura, M., Rahimi, P.M., & Koseoglu, O.R. (2005). Advances in characterization and utilization of asphaltenes. Am. Chem. Soc. 895, 1-17.

Tharanivasan, K. A. (2012). Asphaltene Precipitationfrom Crude Oil Blends, Conventional Oils, and Oils with Emulsified Water. Ph.D. Thesis. Department of Chemical and Petroleum Engineering. University of Calgary, Alberta, Canada.

Welter, K., Salazar, E., Balladores, Y., Marquez, O. P., Marquez, J., & Martinez, Y. (2009). Electrochemical removal of metals from crude oil samples. Fuel Process. Technol., 90 (2), 212-221. in, C., Tan, X., Mu, K., Stryker, J.M., & Gray, M.R. (2008). Associative [pi] - [pi] interactions of condensed aromatic compounds with vanadyl or nickel porphyrin complexes are not observed in the organic phase. Energy&Fuels, 21, 2465-2469.

Natalia Afanasjeva ([section]) *, William H. Lizcano-Valbuena **, Nayeli Aristizabal, Ivone Manozca

* Departamento de Quimica, Universidad del Valle, Cali, Colombia ([section]),,,

Caption: Figure 1. Chemical structure of (a) vanadyl deoxophylloerythroetioporphyrin (VODPEP) and (b) vanadyl benzoetioporphyrin (VOB). (Taken from Fish & Wines, 1984).

Caption: Figure 2. Electrochemical cell a) two compartments and b) three compartments.

Caption: Figure 3. SEM of the graphite bar used as working electrode

Caption: Figure 4. FT-IR of Castilla crude oil asphaltenes

Caption: Figure 5. FT-IR of Castilla crude oil CRA

Caption: Figure 6. Calibration curves for Castilla crude oil: a) vanadium and b) nickel.

Caption: Figure 7. Voltamperogram electrolytic medium THF and C[H.sub.3]CN on Pt electrode at 100 mV/s.

Caption: Figure 8. Voltamperogram electrolytic medium THF and C[H.sub.3]CN on graphite electrode at 100 mV/s.

Caption: Figure 9. Voltamperogram electrolytic medium: a) 0.5% HCl[O.sub.4]/20% C[H.sub.3]OH//0.1M LiCl[O.sub.4]C[H.sub.3]CN (b) electrolytic medium 0.02 MLiCl[O.sub.4]/20% C[H.sub.3]OH//THF of Castilla crude oil. Scan speed 100 mv/s.

Caption: Figure 10. Voltamperogram electrolytic medium 0.02 M LiCI[O.sub.]/20 % C[H.sub.3]OH//THF of Castilla crude oil after (a) 2 hours and (b) 15 hours. Scan speed 100 mv/s.

Caption: Figure 11. Chronoamperometry electrolytic medium 0.02 M LiCI[O.sub.4]/20 % C[H.sub.3]OH//THFof Castilla crude oil
Table 1. Conditions for metal analysis by flame atomic
absorption of Castilla crude oil.

Element         Current   Slit   [lambda]   Relation fuel/oxidant
                (mA)             (nm)

Vanadium (V)    40        0,7    318,4      Acetylene/ Nitrous oxide
Nickel (Ni)     15        0,2    232,0      Acetylene/ Air

Table 2. Data on elemental analysis, H/C relation, empirical formula
and WFEA of asphaltenes and CRA Castilla crude oil

Sample        Mass            Element content (%)

              (mg)   N        H       C       S      O
CRA           2.76   1.54     8.15    84.03   4.01   2.25
Asphaltenes   2.45   1.65     7.48    83.66   4.22   2.98

Sample        Relation H/C   Empirical formula         WFEA (g/mol)

CRA           1.16           [C.sub.63][H.sub.74]NSO   892
Asphaltenes   1.07           [C.sub.59][H.sub.63]NSO   833
COPYRIGHT 2015 Universidad del Valle
No portion of this article can be reproduced without the express written permission from the copyright holder.
Copyright 2015 Gale, Cengage Learning. All rights reserved.

Article Details
Printer friendly Cite/link Email Feedback
Author:Afanasjeva, Natalia; Lizcano-Valbuena, William H.; Aristizabal, Nayeli; Manozca, Ivone
Publication:Ingenieria y Competividad
Date:Dec 1, 2015
Previous Article:Ingenieria y competitividad: logros y retos.
Next Article:Reuso de aguas residuales: impacto en los atributos quimicos y macronutricionales en un suelo inceptisol irrigado con aguas residuales domesticas...

Terms of use | Privacy policy | Copyright © 2019 Farlex, Inc. | Feedback | For webmasters