Understanding Model Crude Oil Component Interactions on Kaolinite

Dec 18, 2017 - Research Institute of Unconventional Petroleum and Renewable Energy (RIUP&RE), China University of Petroleum, East China, Qingdao 26658...
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Understanding model crude oil component interactions on kaolinite silicate and aluminol surfaces: towards improved understanding of shale oil recovery Shansi Tian, Valentina Erastova, Shuangfang Lu, Hugh Christopher Greenwell, Thomas Underwood, Haitao Xue, Fang Zeng, Guohui Chen, Chunzheng Wu, and Rixin Zhao Energy Fuels, Just Accepted Manuscript • DOI: 10.1021/acs.energyfuels.7b02763 • Publication Date (Web): 18 Dec 2017 Downloaded from http://pubs.acs.org on December 20, 2017

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Energy & Fuels

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Understanding model crude oil component interactions on

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kaolinite silicate and aluminol surfaces: towards improved

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understanding of shale oil recovery

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Shansi Tian1,2,3, Valentina Erastova4, Shuangfang Lu1,2*, H. Chris Greenwell3*,

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Thomas R. Underwood3, Haitao Xue1,2, Fang Zeng2, Guohui Chen1,2, Chunzheng

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Wu1,2, Rixin Zhao1,2

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(RIUP&RE), China University of Petroleum (East China), Qingdao 266580,

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Shandong, PR China

Research Institute of Unconventional Petroleum and Renewable Energy

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266580, Shandong, PR China

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Kingdom

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*Corresponding authors: Prof. Shuangfang Lu Research Institute of Unconventional Petroleum and Renewable Energy (RIUP&RE), China University of Petroleum (East China), Qingdao, Shandong, China Phone (or Mobile) No.: +86-18661856596 Email: [email protected] Prof. H. Chris Greenwell Department of Earth Science, Durham University, Durham, United Kingdom Durham University, South Road, Durham, DH1 3LE Phone (or Mobile) No.: +44-01913342324 Email: [email protected]

School of Geosciences, China University of Petroleum (East China), Qingdao

Department of Earth Science, Durham University, Durham, DH1 3LE, United

Department of Chemistry, Durham University, Durham, DH1 3LE, United Kingdom

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ABSTRACT: Shale oil is currently of interest for unconventional resource

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exploration and development. Understanding the mechanism of interaction between

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the complex mixture of organic compounds in shale oil and minerals making up the

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reservoir rock-oil interface will assist recovery. In this study, molecular dynamics

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simulation is used to study the adsorption characteristics of a model oil mixture within

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nanoscale intra-particle pores of kaolinite minerals, which form pore filling structures

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in shale rock. To better understand the effects of oil composition, temperature and

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pressure on the adsorption properties of the model oil mixture, a range of

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temperatures (298 K, 323 K, 348 K and 373 K) and pressures (1 bar, 50 bar, 100 bar

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and 200 bar) representing up to reservoir conditions were used. This study shows that

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adsorption and arrangement of oil molecules is dependent on the surface of kaolinite

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and the distance away from it. The simulations show polar compounds are likely to be

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adsorbed on aluminol kaolinite basal surfaces, while alkanes preferentially adsorb on

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silicate surfaces. In addition, the number of oil molecule bound layers, and total

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adsorption amount on the silicate surface is greater than the aluminol surface. The

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density of adsorbed oil is reduced with increase in temperature, while the effect of

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pressure is not as significant. On the basis of performed molecular simulations, we

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show the adsorption rate of shale oil on the surfaces of kaolinite sheets and assess the

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removable capacity of the model oil.

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Keywords:

shale

oil,

molecular

dynamics,

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clay

mineral,

recovery.

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1. INTRODUCTION

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With increasing demand for energy, and while conventional oil and gas resources are

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depleting, unconventional oil and gas are receiving more attention as they have

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become a major contributor to sustained growth in global hydrocarbon production.

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The exploration and development of shale gas has achieved notable success in North

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America,1-3 and led a global shale gas research boom.4,5 However, with the lessons

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learned from initial phases of shale gas extraction and the decrease of natural gas

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price, investors have now shifted their attention to more profitable shale oil.6-8

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According to the Energy Information Administration,9 in the last 10 years, the

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production of U.S. shale oil has increased 12.2 times to an average of 4.57 million

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barrels per day (MMbbl/d) in 2015, compared to 0.37 MMbbl/d in 2005. Driven by

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the exploitation of tight sand formations, the United States remained the world's top

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producer of petroleum and natural gas hydrocarbons in 2015.10 Shale oil is playing a

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significant role in the global energy industry, and a worldwide shale-oil boom is

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predicted.11-13

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Preliminary evaluation has shown that shale oil resources are very rich in China,

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with the amount of geological resources put at 32 billion barrels, and China ranked

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third among the 41 countries which have an accumulated total shale oil resource of

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345 billion barrels.14 At present, in China, a number of reserves in which the amount

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of geological resources are between 3.5×109 barrels and 7×109 barrels have been

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discovered, for example in the Triassic Yanchang Formation of the Erdos Basin,

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Permian Lucaogou Formation of the Junggar Basin, and the Qingshankou Formation

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of the Songliao Basin. There are also many important discoveries in the lime-shale of

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Bohai Bay area and in the Sichuan Basin.15,16 Compared with marine shale oil in the

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North America, the lacustrine shale oil in China is heavier and has higher amounts of

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polar components; resin and asphaltene is much more abundant than in the North

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America reservoirs. The presence of these components in the lacustrine shale oil is

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thought to result in stronger adsorption of oil within the pores of the shale system,

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which requires extra effort to remove and makes the reservoir more difficult to

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develop. These polar components should be accounted for in the assessment of shale

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oil production in China, as they strongly interact with kerogen, minerals, and the

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widespread nanopores in the shale rock,17-19 leading to errors in recoverable resource

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estimation.

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The adsorption of alkanes on carbonaceous materials, akin to the kerogen, has

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been studied in recent years. McGonigal et al. directly imaged a two-dimensional,

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high-degree ordering of the alkane layer at the liquid/graphite interface using a

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scanning tunneling microscope (STM).20 Castro et al. reported that longer alkanes

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show a strong preference for adsorption onto graphite.21 Furthermore, Severson and

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Snurr studied the adsorption isotherms of linear alkanes (ethane, pentane, decane, and

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pentadecane) on activated carbon and evaluated the functions of pore size, chain

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length, and temperature on adsorption.22 Recently, Harrison et al. studied the single

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component preferential adsorption of linear and branched alkanes in pores with

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different apertures (1, 2, and 4 nm) at 390 K.23

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A similar issue of accounting for hydrocarbons trapped in narrow pores for shale

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gas has been discussed by Ambrose et al., who suggested that an adjustment of

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adsorption phase volume is necessary for gas-in-place (GIP) calculations, leading to a

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10 to 25% decrease in GIP in comparison with the conventional method for 4

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assessment.24-26 In addition, Wang reported that the unrecoverable fraction of oil-in-

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place (OIP) is 13% in Bakken shale,27 when taking the adsorption of alkanes in a

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graphite model into consideration. Nevertheless, there are relatively few studies that

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explore the effect of polar component adsorption on the estimation of shale oil-in-

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place.

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While the interaction of hydrocarbon molecules with pores and surfaces coated

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with kerogen like materials has been more extensively studied, conceptually shale

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consists of two parts: organic matter (kerogen) and inorganic matter (minerals). The

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inorganic part of shale mainly contains quartz, calcite, feldspar and clay minerals.

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Each kind of mineral makes up a certain volume fraction of a lacustrine/marine shale

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and plays an important role in shale systems through presenting intra- and inter-

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particle pore networks that may hold hydrocarbons. Studying the interface of

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inorganic pores with oil is challenging, and computational chemistry simulations offer

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great potential to examine the properties of mineral interfaces and oil mixtures at an

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atomistic level. Previous simulation studies of mineral-organic interfaces have been

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widespread and extensively studied in the past, such as quartz,28-30 calcite,31

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montmorillonite,32 kaolinite,33 and muscovite.34

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Kaolinite often forms surface coatings in the inorganic pores of shale reservoirs,

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as well as forming pore filling aggregates and presents inter-particle and intra-particle

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pore surfaces. Kaolinite is different from certain other clay minerals such as illite,

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smectite, and chlorite due to the octahedral-tetrahedral structure presenting two

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different surfaces, the mainly oil-wetting silicate surface and the water-wetting

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aluminol surface. A significant number of computational studies have been published

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on kaolinite surfaces,33,35-44 but these have primarily focused on the adsorption 5

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mechanisms of either a single molecule, or a relatively small number of organic

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molecules to the mineral. As shale oil contains different types and molecular weight

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alkanes, aromatic hydrocarbons and polar compounds, it is important to study the

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adsorption of different alkanes in the presence of aromatic and polar compounds to

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build up a more complete picture of the mineral-oil interface. In addition, temperature

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and pressure change with depth and maturity in a shale reservoir, therefore it is also

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important to take these into consideration when considering shale oil adsorption.

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In this present study, the adsorption behavior of a simple 6-component model

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crude oil mixture on kaolinite basal surfaces (to represent a shale component) was

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studied under reservoir conditions using molecular dynamics (MD) simulations. The

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main objectives were: (1) to provide nanoscale molecular-level resolution for studying

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the interactions at the hydrocarbon-shale interface; (2) to accurately characterize the

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adsorption properties of alkanes/polar compounds in the mineral slit-shaped pore

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space under different temperatures and pressures; (3) to provide improved parameters

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for the calculation of the unrecoverable fraction for shale OIP (oil-in-place)

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estimation.

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2. MODELS AND SIMULATION DETAILS

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The kaolinite unit cell has the chemical formula Al2Si2O5(OH)4, without isomorphic

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substitutions. The initial atomic positions were taken from the AMCSD (American

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Mineralogist Crystal Structure Database).45,46 This was converted to a cubic cell. The

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model contained three periodically replicated sheets of kaolinite, creating a clay slab

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of 252 unit cells (12×7×3) as shown in Figure 1g, with dimensions of approximately

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6.2×6.3×1.9 nm. The kaolinite structures initially occupied the region 0