International Journal of Analytical Chemistry

Volume 2016 (2016), Article ID 4182164, 7 pages

http://dx.doi.org/10.1155/2016/4182164

## Study on Colloidal Model of Petroleum Residues through the Attraction Potential between Colloids

^{1}College of Science, China University of Petroleum (East China), Qingdao, Shandong 266555, China^{2}State Key Laboratory of Heavy Oil Processing, China University of Petroleum (East China), Qingdao, Shandong 266555, China

Received 2 December 2015; Revised 2 March 2016; Accepted 3 March 2016

Academic Editor: Neil D. Danielson

Copyright © 2016 Long-li Zhang et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

#### Abstract

The samples of DaGang atmospheric residue (DG-AR), Middle East atmospheric residue (ME-AR), TaHe atmospheric residue (TH-AR), and their thermal reaction samples were chosen for study. All the samples were fractioned into six components separately, including saturates plus light aromatics, heavy aromatics, light resins, middle resins, heavy resins, and asphaltenes. The dielectric permittivity of the solutions of these components was measured, and the dielectric permittivity values of the components can be determined by extrapolation, which increased steadily from saturates plus light aromatics to asphaltenes. Moreover, the Hamaker constants of the components were calculated from their dielectric permittivity values. The Van der Waals attractive potential energy between colloids corresponding to various models could be calculated from the fractional composition and the Hamaker constants of every component. It was assumed that the cores of colloidal particles were formed by asphaltenes and heavy resins mainly; the other fractions acted as dispersion medium. For the three serials of thermal reaction samples, the Van der Waals attraction potential energy between colloids for this kind of model was calculated. For TH-AR thermal reaction samples, the Van der Waals attraction potential energy presented the maximum as thermal reaction is going on, which was near to the end of coke induction period.

#### 1. Introduction

Petroleum residues are found to be colloidal systems, and asphaltenes are considered to be the cores of them [1–3]. Asphaltenes, which are the heaviest and the most polar fraction in residue, play a key role in the processing of heavy oil. The destruction of colloidal stability of heavy oil induces asphaltene precipitation and causes troubles to many petroleum processes including production, transportation, or refining.

Since the colloidal stability plays an important role in the usage of heavy oil, the colloidal model and colloidal stability of heavy oil have been widely studied. Because petroleum residue is a kind of complicated mixture, composed of innumerable molecules, it has to be divided into fractions based on polarity and solubility difference for further study [4–6]. Based on the solubility difference and chromatography separation, the former researchers found that the polarity of residue fractions increased steadily as the following sequence: saturates plus light aromatics, heavy aromatics, light resins, middle resins, heavy resins, and asphaltenes [7, 8]. The fractions distribution of residue played an important role in the colloidal stability, the reaction characteristics, and the emulsification performance of residue [9].

Although many researchers have presented various micelle models for residue, there are no models based on the direct potential energy between colloids derived from the composition and characteristics of fractions. Moreover, the colloidal stability is influenced by the fractions distribution and the characteristics of heavy oil [10–13]. The mean dipole moment of the fractions can be measured [12]. For example, the researchers pointed out that SARA composition influenced the stability of asphaltenes in heavy oil [14–16]. But SARA composition partition is blurry, based on the solubility and polarity of molecules, and every fraction was a complicated mixture. Although the contents and the characteristic of SARA fractions determine the colloidal stability of heavy oil together, the relationship between them cannot be forecasted integrally and quantitatively.

Some researchers pointed out that resins were helpful to the stability of asphaltenes [15, 16], so the increase of resin content would enhance the colloidal stability of heavy oil, and the increase of asphaltenes content would decrease the colloidal stability. It should be noted that resins are not required in order for asphaltenes to form stable nanocolloidal suspensions in toluene. As the division of asphaltene and resin is based on solubility, the characteristics of resin are adjacent to that of asphaltenes, and the characteristics of them are continuous. If the properties of the molecules are just on the critical point of asphaltenes and resins, it is difficult to deduce the effects of these molecules on the colloidal stability of residues, since this statement is qualitative and does not integrate the effect of properties and the composition of fractions of residue at the same time.

According to “the modified Yen model” proposed by Mullins and coresearchers [14], the asphaltene colloidal particles in crude oils were nanocolloidals, which were mainly composed of asphaltenes and the heaviest resins. The asphaltenes were in hierarchical structures in crude oils, such as molecules, nanoaggregates, and clusters of nanoaggregates. This work will study the attractive energy between the clusters dispersed in the medium of other fractions.

The colloidal stability of heavy oil is affected by the attractive potential and repulsive potential between colloid groups. This paper is to instruct the colloidal model of residue based on the attractive potentials between colloids for the sake of viewing the fractions distribution and fraction characteristics. This model will be used to reveal the colloidal stability variation during thermal reactions.

#### 2. Experimental Section

There are three kinds of atmosphere residues studied, the boiling point of which was more than 350°C. The samples were DaGang atmospheric residue (DG-AR), Middle East atmospheric residue (ME-AR), and TaHe atmospheric residue (TH-AR). Their properties have been presented in the previous papers [8, 12].

The samples were upgraded to study the colloidal stability variation of residues during thermal reaction. Thermal reaction was performed under nitrogen and the initial pressure is 1.0 MPa at room temperature. The coke induction period of thermal reaction was 80 min for DG-AR at 405°C, 100 min for ME-AR at 400°C [12], and 60 min for TH-AR at 400°C. The heavy oil was separated into n-pentane asphaltene and n-pentane maltene. Then, the maltene was separated into fractions through liquid chromatographic separation; and the neutron aluminum oxide was used as adsorbent, which was pretreated and contained 5% wt. water [13]. The eluting solvents used were n-heptane, mixture of n-heptane and benzene (v : v = 85 : 15), mixture of n-heptane and benzene (v : v = 1 : 1), benzene, or mixture of benzene and ethanol (v : v = 1 : 1). The corresponding fractions could be gained as the following: saturates plus light aromatics, heavy aromatics, light resins, middle resins, and heavy resins. The colloidal stability variation of residue came from the shift of fractions distribution and the molecular characteristics of every fraction [8, 12].

The separation scheme, mean molecular weight, and the dielectric permittivity measuring methods were the same as described previously [8, 12, 13].

The fractions were diluted by benzene separately. Firstly, a stock solution of fraction was prepared. Then, the stock solution was distributed in vials, and benzene was added to each vial to achieve the preconcerted weight percentage. The solution was placed at least for 24 hours before measurement to ensure stabilization. The dielectric permittivity of the solutions of fractions was measured, and the dielectric permittivity of fractions can be gained when extrapolated to the 100%. The frequency used for permittivity measurements was 1 kHz. The Hamaker constants of the fractions were calculated from the dielectric characteristics of them. When the dielectric permittivity value is little, there are not notable differences between the long-range and the short-range Hamaker constant. The dielectric permittivity values of the components of petroleum residue were lower than 10. So the short-range Hamaker constant was used in this study. When the two particles were the same and existed in vacuum, the short-range Hamaker constant can be calculated as [19] is the extrapolated relative dielectric permittivity of certain fraction; is the characteristic absorption frequency; is the characteristic absorption wavelength, nm; is the Planck constant, J·s; is the velocity of light, m·s^{−1}.

Since the fractions of petroleum residue were complex mixture, the UV-vis absorption spectrum of them was wideband from 200 nm to 400 nm without specific fine structures [20], the characteristic absorption wavelength for fractions of petroleum residue was chosen as 300 nm. The Hamaker constants of fractions could be computed by (1). The researchers have proposed various colloidal model of residue [14, 17, 18]. The Van der Waals attraction potential energy of different model could be calculated from the fractional composition and the Hamaker constants of every component.

#### 3. Results and Discussions

##### 3.1. The Dielectric Permittivity of the Solutions of Fractions

The dielectric permittivity of the solutions of fractions was measured. The asphaltene of TH-AR thermal reaction sample for 40 minutes was illustrated, as exampled. It could be seen from Figure 1 that the dielectric permittivity of solution increased with concentration, and the value for the neat material can be determined by extrapolation to 100%, which was 7.75. The dielectric permittivity of other samples could be gained also and shown in Tables 1–3.