GR/N21482 Feasibility of design methods for asphaltenes 1/6 FEASIBILITY OF EXPLOITING COMPUTATIONAL DESIGN METHODS TO DEVELOP NOVEL ASPHALTENE INHIBITORS Final Report 1 Summary This project was a ROPA award for a feasibility study into the scope for exploiting molecular modelling to understand asphaltene deposition and design better prevention strategies. Of particular interest was to determine whether full-scale atomistic modelling of asphaltene aggregation—including explicit solvent—was now viable. This was a 15 month study, and was a major new research initiative. The results of the study have been extremely promising. Fully atomistic molecular dynamics simulations of the small aggregates that form as the first stage in asphaltene deposition and immersed in realistic solvents have been shown to be viable. Most importantly, the stability of these primary particles has been shown to be assessable from multi-nanosecond simulations; such simulations can be performed in a reasonable time on a modest, modern linux cluster. Further, the difference in stability induced by solvents such as heptane (which fosters precipitation) and toluene (which promotes solubility) were correctly reproduced. Thus this project has established that reliable simulations of asphaltene aggregation / dispersion can be performed at a molecular level, and that the scale of the simulations is such that they can readily be extended to consider the influence of natural resins or potential inhibitors. This proof of concept has already attracted interest from the oil industry. 2 Background/Context The exploration, production and transportation of crude oils is beset with a number of problems arising from the deposition of unwanted solids. Probably the most intractable of these is the precipitation of asphaltenes, which can occur at any stage of oil production and can be responsible for blocking pipes and well heads. The term asphaltenes refers to a highly complex mixture of heavy organic residues composed of fused aromatic and heterocyclic rings together with paraffinic side chains. They are usually strongly polar; contain a significant percentage of hetero-atoms, particularly sulphur; and may contain traces of metals such as vanadium and nickel. Asphaltene precipitates usually form as either a tarry solid or a sludge, both of which forms can seriously impair the flow of other fluids and can be very difficult to remove. As a consequence it is desirable to be able to predict the likelihood of asphaltene deposition occurring so that appropriate dispersants can be added in advance. Unfortunately, the theory for asphaltene precipitation is not yet adequate. Nor is there a sufficient understanding of the process to adopt a rational approach to developing more effective dispersants and inhibitors. The major barrier to both of these goals is probably the lack of a molecular-level characterisation of the secondary structure in asphaltenes. There is a reasonably good knowledge of their chemical composition1—individual molecules can be characterised by planar sheets of polar, aromatic groups, edged by aliphatic side chains—although any particular asphaltene sample will be a heterogeneous mixture of compounds that fit this general description. There is also some information about the nature of the aggregation process. In particular, X-ray diffraction studies2 indicate that the aggregation is a two-step process as illustrated in Figure 1. GR/N21482 Feasibility of design methods for asphaltenes 2/6 Figure 1: Schematic of the deposition process. (Taken from Brandt et al., J. Phys. Chem., 1995, 99, 10430) However, there are still fundamental questions about the conformation of the individual stacks (or primary particles), their form when in the oil phase, the nature of the forces that lead to flocculation, and how these may arise from conformational changes induced by variations in the temperature or composition of the oil. Such issues need to be addressed before a reliable theory can be developed, and before a rational approach to developing better dispersants can be adopted. Although computer modelling has proved to be an ideal tool for providing exactly this type of information in many other applications, only simplified studies of asphaltenes had been performed prior to this project.3 There had been some energy minimisation calculations, but applications of the more sophisticated statistical mechanical techniques were essentially absent. Most importantly, there had been no serious attempt to include solvent effects; yet solvent effects clearly make the difference between dissolution and deposition. Indeed, a working definition of asphaltenes is: that component of a crude oil that precipitates when heptane is added to a solution of the oil in toluene. The purpose of this project was, therefore, to determine whether the considerable advances made in molecular simulation of materials and biomolecules could now be extended to provide realistic molecular models of asphaltene deposition as well. In particular, to assess whether molecular dynamics simulations with explicit solvent were an appropriate tool for studying the early stages of Figure 1. 3 Key Advances and Supporting Methodology AIMS AND OBJECTIVES As outlined in the original report, the aim of this project was to assess the feasibility of using rigorous molecular simulation methods to study the precipitation of asphaltenes from oil. Such simulations would provide invaluable information for developing effective asphaltene prevention technologies, but only if the simulations could be made sufficiently realistic. This project was funded to perform exploratory simulations using a fully atomistic model of asphaltenes in heptane and toluene in order to quantify the resources needed for a full-scale modelling study and indicate the type information that could be obtained. These objectives have been realised in full during this project. Atomistic molecular dynamics simulations have been performed on collections of asphaltene molecules in the specified solvents. Our work has demonstrated that aggregation / dispersion of asphaltene molecules is seen on the timescale accessible to such simulations (ca. 10–8 s using modern GR/N21482 Feasibility of design methods for asphaltenes 3/6 linux clusters) and that the solvent effects are correctly reproduced in at least a semiquantitative manner: small aggregates of 2 and 4 asphaltene molecules are found to be stable in n-heptane, but to disperse in toluene at temperatures around 300 K. We have also confirmed that such simulations can provide information about the energetics of aggregation, the solvent structure and dynamics that facilitate it, and the fundamental intermolecular interactions that drive it. In summary, this study has verified that a full scale simulation of asphaltene deposition is now feasible, and can provide reliable information about the molecular mechanisms of asphaltene aggregation that would be extremely useful in devising inhibition strategies. DETAILED RESULTS Simulation Methodology The asphaltene was constructed with a composition typical of those analyses published in the literature: the polyaromatic sheet consisted of 10 fused phenyl rings and two aromatic heterocycles, supplemented with two aliphatic cycles and 5 aliphatic side chains with typically 4–6 heavy atoms; both sulphur and nitrogen were present (see Figure 2). Stacks of both 2 and 4 asphaltene molecules were constructed within the Quanta/CHARMm package by using both constrained molecular dynamics (in vacuum) and manual docking. Initially, a number of potential dimer conformations were constructed. The lowest energy of these were then subjected to extensive annealing to ensure that the stacks would remain stable at 300 K in vacuum. Several different dimer conformations were then selected for use in the solvated simulations. Asphaltene tetramers were constructed from two dimers, with a somewhat less extensive annealing process. The asphaltene stacks were solvated by embedding them in a solvent box obtained from an MD simulation of the neat solvent, and removing solvent molecules that overlapped with the asphaltenes. NPT MD simulations were then carried out at 0.02 MPa and 300 K, with the asphaltene stack treated as a rigid body, in order to relax the solvent to an appropriate density. About 200 ps simulations were required for this. Finally, about 2 ns simulation time was accumulated in which the asphaltene was treated as a fully flexible molecule. Solvating the dimers required 255 heptane molecules or 329 toluene molecules in a simulation box of length ca. 35 Å. For the tetramer, 482 heptane or 484 toluene molecules were used with the resulting simulation box being about 50 Å. Several different initial dimer geometries and one tetramer geometry were simulated in both solvents. All atom potentials (CHARMm 27 force field) were used throughout, and electrostatic interactions were evaluated with an EWALD sum. All solvated simulations were performed with DL_POLY. Results & Feasibility Two of the key issues to be addressed in this feasibility study were (i) whether the dynamics that characterise asphaltene aggregation and dispersion are accessible on the MD timescale (ca. 10-8 ps), and (ii) if so, whether the atomistic simulations can correctly reproduce the observed solvent effects. The latter is particularly important, since if the simulations cannot reproduce the difference between heptane (which induces aggregation) and toluene (which promotes solubility), then they can say nothing reliable about strategies for inhibiting asphaltene deposition. The results of this study were very promising on both counts. In general, the dimeric stacks showed clear evidence of decomposing in toluene on a nanosecond timescale, but no such decomposition was evident in heptane. As an example, snapshots of the asphaltene stack after 2 ns from one of the dimer simulations are given in Figure 2. The initial dimer geometry was very similar to the left hand structure in Figure 2, with the aromatic sheets forming a GR/N21482 Feasibility of design methods for asphaltenes 4/6 slipped parallel arrangement with about 25% overlap of the planar sheet and an inter-sheet distance of 3.8 Å; this geometry is characteristic of strong π-stacking interactions. For the simulation in heptane (left hand picture) the dimer showed no indication of instability throughout the simulation. Indeed, if anything the stack became more stable, with the intersheet distance decreasing to 3.5 Å; the overlap of the aromatic sheets and their relative orientation showed no observable variation during the simulation. In contrast, there is clear evidence of structural changes for the same dimer in toluene. After 2 ns the two aromatic sheets were clearly not parallel, and there was no longer any significant overlap of the aromatic regions. The rate of this decomposition was found to depend on the initial configuration of the dimer, but was typically observable on a ns timescale. Figure 2: asphaltene dimers after 2 ns simulations in heptane (left) or toluene (right). In both cases the initial conformation looked very similar to that on the left. Grey indicates C atoms, yellow S and blue N. Simulations with the tetramers confirmed these trends. As the calculations were intended to be indicative rather than definitive, less effort was made to anneal the starting structure of the tetramer than was the case with the dimers. While the tetramer was built from two well-annealed dimers, some strain did remain in the packing of the two dimers, which lead to some disordering of the tetramer in heptane. None-the-less, strong evidence of favourable π-stacking interactions between the asphaltene molecules was retained in heptane, but completely absent in toluene. Some factors that can affect the stability of the stacks emerged from this preliminary study and warrant further investigation. (1) The role of the solvent: Close examination of the simulations indicated that toluene can effectively substitute for the asphaltene on the aromatic stacks, and thereby gradually displace the π-stacking interactions between the asphaltenes. Indeed, average 3-D distributions of toluene about the asphaltene showed that the toluene binds most strongly, and aligns best with the aromatic sheets, precisely in the region where the aromatic sheets originally overlapped. It is likely that resins, which act as natural dispersants, will have a similar effect on the asphaltene stacks and would be amenable to molecular simulation along the lines illustrated in this project. (2) The aliphatic side chains: The location and dimensions of the aliphatic side chains was found to be a limiting factor for the size of asphaltenic stack that could be built. At the same time, the side chains appeared to provide some protection to the stack in heptane, wrapping around the stack and restraining the relative motion of the aromatic sheets. The distribution of chain lengths and locations in a crude oil is likely to have a considerable effect on the ease of aggregation and the nature of any inhibitors that would be needed. GR/N21482 Feasibility of design methods for asphaltenes 5/6 Resource Implications The 2 ns simulation of an asphaltene tetramer in heptane took about 1 month on an 8 processor PIII/866 MHz cluster. Simulations of the tetramer in toluene were about 30% faster, but the later stages of the dissolution process were found to be hindered by the size of the simulation box, and so larger system sizes would be desirable. While this is clearly a nontrivial exercise, and will not yet allow computational screening for new inhibitors, this project has shown it to be a viable method for obtaining detailed mechanistic information at a molecular level. Such information is not available from experimental sources. The computational resource is, itself, quite modest now and so more complex simulations can be envisaged. In particular, potential of mean force studies of the addition of asphaltene molecules to form the primary stacks, and on the interaction between two stacks (i.e. the first and second stage equilibria in Figure 1) have been shown by this project to be viable. Some development of coarse-grained potentials for asphaltenes—along the lines that have already been used for polymer and biomembrane simulations—would be useful in extending the timescale on which the aggregation can be followed. However, in the final analysis this project has shown that existing methods and potentials are sufficient to allow realistic molecular simulations of the molecular processes that underlie asphaltene precipitation. 4 Research Impact and Benefits to Society The ability to control asphaltene deposition is important for oil drilling and transport, and oil companies currently have large capital and operating costs associated with trying to alleviate the problems they cause. Also, many of the long-term environmental problems arising from oil spills are related to the asphaltene deposition that occurs as the oil spillages. Given the complexity and inhomogeneity of the compounds involved, this is a very difficult problem and a complete solution will only result from the synthesis of a large number of different research studies. This project has succeeded in highlighting molecular modelling as potentially a very powerful tool to add to the methods that are already being used to solve this problem. The success of this project in achieving this aim, and the impact of the results on the oil and gas industry, can best be seen from the continuing positive response from a number of different sectors of the oil industry to the PI’s research. In particular, the PI has agreement in principle from an Algerian oil company to fund a start-up molecular modelling study on their asphaltenic crude oils. Further, an extended research contract with Cabot Specialty Fluids (USA) and a new research contract with Lubrizol were obtained partly due to the greater breadth of oil-related expertise the PI could offer as a result of this project. 5 Dissemination Activities and Further Research This project was a 15 month feasibility study, and represented a major new initiative. So far the results have been presented at one international RSC conference on Chemistry in the Oil Industry. The work will also be presented at the international conference on Heavy Organics Deposition in Mexico, November 2002. Both of these conferences have a high profile in the oil industry, and so are a very effective means of targeting the key group of beneficiaries identified in the original proposal. Dissemination is also being achieved through publication in the Journal of Physical Chemistry, and Energy & Fuel; the former targets the relevant academic community while the latter is probably the most appropriate journal for reaching the oil industry. This work has also been publicised informally via the PI’s contacts in a number of relevant industrial organisations, including BP Exploration, Cabot Specialty Fluids (UK), Conoco, TROSS, Statoil and Exxonmobil. GR/N21482 Feasibility of design methods for asphaltenes 6/6 As a direct result of these activities, the PI was approached by Sonatrach/CRD (Algeria), and discussions are now underway with a view to molecular modelling studies of asphaltene inhibition in Algerian crude oil. Research is still in progress on a number of the avenues identified in this feasibility study. Initial work will focus on potential of mean force calculations for the aggregation of two asphaltene stacks. Pending a successful outcome to the talks with Sonatrach/CRD, we will also perform studies to characterise aggregation of asphaltenes with a different chemical composition to that considered in this feasibility study. A grant application for a full-scale study, focusing on aggregation in the presence of resins, will be submitted to the EPSRC later this year. References 1 2 3 J. Christopher, A.S. Sarpal, G.S. Kapur, A. Krishna, B.R. Tyagi, M.C. Jain, S.K. Jain, A.K. Bhatnagar, Fuel, 75, 999 (1996); J.C. Delrio, R.P. Philp, J. Allen, Org. Geochem., 18, 541 (1992) H.C.A. Brandt, E.M. Hendriks, M.A.J. Michels F. Visser, J. Phys. Chem., 99, 10430 (1995) ;N.F. Carnahan, L. Quintero, D.M. Pfund, J.L. Fulton, R.D. Smith, M. Capel, K. Leontaritis, Langmuir, 9, 2035 (1993) J. Murgich, J.A. Abanero, O.P. Strausz, Energy & Fuels, 13, 278 (1999); J. Murgich, J.M. Rodriguez, Y. Aray, Energy & Fuels, 10, 68 (1996); E. Rogel, Colloids and Surfaces, 104, 85 (1995)