<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article  PUBLIC "-//NLM//DTD Journal Publishing DTD v3.0 20080202//EN" "http://dtd.nlm.nih.gov/publishing/3.0/journalpublishing3.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" dtd-version="3.0" xml:lang="en" article-type="research article"><front><journal-meta><journal-id journal-id-type="publisher-id">OJOGas</journal-id><journal-title-group><journal-title>Open Journal of Yangtze Oil and Gas</journal-title></journal-title-group><issn pub-type="epub">2473-1889</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/ojogas.2017.23013</article-id><article-id pub-id-type="publisher-id">OJOGas-77630</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Engineering</subject></subj-group></article-categories><title-group><article-title>
 
 
  Evaluation of the Effects of Alcohol on De-Emulsification of Niger Delta Crude Oil Using Commercial De-Emulsifiers
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>K.</surname><given-names>C. Igwilo</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>S.</surname><given-names>T. A. Okolie</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>P.</surname><given-names>A. L. Anawe</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Ogbudu</surname><given-names>Roland</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Jude</surname><given-names>Odo</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib></contrib-group><aff id="aff2"><addr-line>Covenant University, Ota, Nigeria</addr-line></aff><aff id="aff1"><addr-line>Federal University of Technology, Owerri, Nigeria</addr-line></aff><aff id="aff3"><addr-line>Chevron Oil and Gas Company, Lagos, Nigeria</addr-line></aff><author-notes><corresp id="cor1">* E-mail:<email>meetkevin2006@yahoo.com(KCI)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>14</day><month>07</month><year>2017</year></pub-date><volume>02</volume><issue>03</issue><fpage>168</fpage><lpage>175</lpage><history><date date-type="received"><day>April</day>	<month>6,</month>	<year>2017</year></date><date date-type="rev-recd"><day>Accepted:</day>	<month>July</month>	<year>11,</year>	</date><date date-type="accepted"><day>July</day>	<month>14,</month>	<year>2017</year></date></history><permissions><copyright-statement>&#169; Copyright  2014 by authors and Scientific Research Publishing Inc. </copyright-statement><copyright-year>2014</copyright-year><license><license-p>This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/</license-p></license></permissions><abstract><p>
 
 
  This research work evaluates the effects of alcohol on de-emulsification of Niger Delta crude oil using RP6000 and Chimec 2439 as de-emulsifiers. The laboratory measurements were carried out as per API standard. Stable emulsion was prepared using brine. The samples were de-emulsified. Methanol and ethanol were added respectively, with water and without water as modifiers. The measurements of the effect of adding alcohols on water separation efficiency were carried out using methanol to water ratio, M = 4:1 and ethanol water ratio, E = 4:1. The results show that solubility with alcohol is greater in emulsion than the solubility of alcohol without water. Some comparisons were also made based on the plots on percent water separation versus time for the two modifiers and de-emulsifiers. The maximum separation efficiency of 61% was obtained at concentration of 25% methanol, 75% RP6000, 20 ppm and Chimec 2439 gave maximum separation efficiency of 56.6% at concentration of 75%, 20 ppm at 120 minutes. Based on the results, methanol therefore gave larger effect on water separation efficiency than ethanol.
 
</p></abstract><kwd-group><kwd>De-Emulsification</kwd><kwd> Niger Delta Crude Oil</kwd><kwd> RP6000</kwd><kwd> Chimec 2439</kwd><kwd> Methanol</kwd><kwd> Ethanol</kwd><kwd> Separation Efficiency</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Emulsion is a heterogeneous system, containing at least immiscible liquid intimately dispersed in another in the form of droplets with a diameter, in general, ranging between (0.1~20) microns, and it is stabilized by an emulsifying agent, asphaltenes, resins and finely divided solids. The dispersed droplets are known as the internal phase. The liquid surrounding the dispersed droplets is the external or continuous phase. The emulsifying agent separates the dispersed droplets from the continuous phase [<xref ref-type="bibr" rid="scirp.77630-ref1">1</xref>] . Water-in-oil emulsion is formed during the production of oil, which is often accompanied with water. The stability of the emulsion is ranging from a few minutes to years depending on the nature of the crude oil [<xref ref-type="bibr" rid="scirp.77630-ref2">2</xref>] . Crude oils consist of, in any case, a series of hydrocarbons such as alkenes, naphthenes, and aromatic compounds as well as phenols, carboxylic acids, and metals. A major fraction of sulfur and nitrogen compounds may be present as well. The carbon numbers of all these components range from 1 (methane) through 50 or more (asphaltenes). Some of these components (asphaltenes, resins, wax, and naphthenic acids) can form films at oil surfaces. So, the tendency to form stable or unstable emulsions of different kinds varies greatly among different oils [<xref ref-type="bibr" rid="scirp.77630-ref3">3</xref>] . The natural petroleum emulsion resulting from the secondary production consists of crude oil as dispersion medium and brine as dispersed phase, normally stabilized by natural chemicals such as asphaltenes, resins, and solids such as clays and waxes [<xref ref-type="bibr" rid="scirp.77630-ref2">2</xref>] .</p><p>Emulsions are undesirable because the volume of dispersed water occupies space in the processing equipment and pipelines, increased operating and capital costs. Moreover, the characteristics and physical properties of oil change significantly on emulsification. Emulsion resolution is therefore an important element in handling the petroleum, from the time it is produced until it enters the refining process. In order to minimize the production problems related with crude oil emulsions and environmental concerns, petroleum operators need to prevent emulsion formation or to break it [<xref ref-type="bibr" rid="scirp.77630-ref4">4</xref>] . The treatment of water-in-crude oil emulsions involves the application of mechanical, thermal, electrical, and chemical processes [<xref ref-type="bibr" rid="scirp.77630-ref5">5</xref>] . Chemical method of resolving crude oil emulsions are based on the addition of reagents (de-emulsifiers) which destroy the protective action of hydrophobic emulsifying agents and allow the water droplets to coalesce. There are anionic, cationic and nonionic surfactants that have been used as de-emul- sifiers [<xref ref-type="bibr" rid="scirp.77630-ref6">6</xref>] . Success of chemical de-emulsifying method is dependent upon the adequate quantity of a properly selected chemical that must be added into the emulsion, through mixing of the chemical with the emulsion, adequately heat may be required to facilitate or fully resolve an emulsion. De-emulsifiers permit agglomeration, coalescence and gravity settling of the water droplets [<xref ref-type="bibr" rid="scirp.77630-ref7">7</xref>] . The formulation of commercial de-emulsifiers is largely based on empirical approaches in an attempt to get the effective agent, which can work in shorter separation times and smaller dosages [<xref ref-type="bibr" rid="scirp.77630-ref6">6</xref>] . In the petroleum industry the usual emulsions encountered are water droplets dispersed in the oil phase and termed as water-in-oil emulsion (W/O), conversely, if the oil is the dispersed phase, it is termed oil-in-water (O/W) emulsion. In addition to the usual emulsion types, multiple emulsions for instance, water droplets dispersed in oil droplets that are in turn dispersed in a continuous water phase (W/O/W) can occur.</p><p>Emulsion Stability is widely used to refer to the persistence of an emulsion in the environment, and has been identified as an important characteristic of water-in-oil emulsions. Some emulsions quickly decompose into separate oil and water phases once removed from the sea surface, while more stable emulsions can persist for days to years. Recent work indicates that the viscosity of an emulsion is related to its stability [<xref ref-type="bibr" rid="scirp.77630-ref8">8</xref>] . Crude oil is found in the reservoir in association with gas and saline formation water. The numbers of wells now co-producing water with crude oil is steadily increasing, these immiscible fluids are readily emulsified by the simultaneous action of pressure drop at the well head [<xref ref-type="bibr" rid="scirp.77630-ref9">9</xref>] . The knowledge of the properties and characteristics of the emulsion and the mechanisms that are taking place during coalescence of water droplets are required for fast separation [<xref ref-type="bibr" rid="scirp.77630-ref10">10</xref>] .</p><p>De-emulsifiers are molecules that aid the separation of oil from water usually at low concentrations. They prevent formation of water in oil mixture. The structures of de-emulsifiers are not easily categorized as emulsifiers. Some de-emulsifiers are polymers; others have structures similar to non-ionic emulsifiers. De-emulsifiers are surfactants that are important in breaking the emulsion system [<xref ref-type="bibr" rid="scirp.77630-ref11">11</xref>] .</p><p>The best de-emulsifiers are one that can reduce the interfacial shear viscosity increases the interfacial mobility and destabilizing the water-oil emulsion. To ensure the high quality performance, a de-emulsifier should possess the following characteristics [<xref ref-type="bibr" rid="scirp.77630-ref12">12</xref>] : 1) The de-emulsifier should be able to partition into the water phase and oil phase 2) Dissolved in the oil phase 3) The concentration of the de-emulsifier in the droplet must be sufficient to ensure a high enough diffusion flux to the interface.</p><p>The de-emulsifier must be high enough to suppress the interfacial tension gradient, thus accelerating the rate of film drainage hence promoting coalescence. Dodd [<xref ref-type="bibr" rid="scirp.77630-ref13">13</xref>] in 1954, concluded that the de-emulsifiers that are soluble in both phases are effective in breaking crude oil emulsions, provided that very small amounts of hydrochloric or Sulfuric acid are also added. He suggested the use of Phenol and Sulfuric acid. Hanapi [<xref ref-type="bibr" rid="scirp.77630-ref14">14</xref>] in 2006, investigated that the combination of oil soluble de-emulsifiers and water-soluble de-emulsifiers produced great result in water separation. He also observed that the formulation de-emul- sifiers is better than other commercial de-emulsifier.</p></sec><sec id="s2"><title>2. Materials and Methodology</title><p>The aim is to experimentally investigate the effect of de-emulsifier concentration, separation time and modifier agent to break crude oil emulsion. The main purpose of the research is to know the degree of the effectiveness of methanol and ethanol to emulsion de-emulsifiers. Two commercial de-emulsifiers were used: RP6000 and Chimec 2439. Chemical method was applied in breaking crude oil emulsion.</p><sec id="s2_1"><title>2.1. Apparatus Used in Experiments</title><p>The equipment used were:</p><p>1) Water bath with temperature controller type (Haak-G and Haak-D)</p><p>2) Water bath type (Gerhardt Bonn EV2) connects with thermocouple.</p><p>3) Batch reactor with stirrer.</p><p>4) Electrical mixer with standard turbine impeller type (RL10 M 24684). The mixer calibrated using Dual Digital Tachometer (DT-2268) made in Germany.</p><p>5) Electronic balance type (Ntrols mod. Mark 2200) with &#177;0.05 g accuracy.</p><p>6) Clock timer.</p><p>7) Thermometer.</p><p>8) Cylinders (10 ml) and Beakers (100 ml).</p><p>9) Separator funnel.</p><p>10) Burette.</p></sec><sec id="s2_2"><title>2.2. Materials</title><p><xref ref-type="table" rid="table1">Table 1</xref> below shows the Niger Delta crude oil sample. Their laboratory measurements were carried out and the physical properties as stated in the table were obtained. This is 28.6˚ API crude oil with minimum salt, water and sediment contents of 0.0007% and 0.046% respectively. Asphaltene and sediments help to stabilized the emulsion during emulsification before being de-emulsi- fied.</p></sec></sec><back><ref-list><title>References</title><ref id="scirp.77630-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Lissant, K.J. (1988) Emulsification and De-Emulsification, a Historical Overview. Colloids and Surfaces, 29, 15. https://doi.org/10.1016/0166-6622(88)80168-9</mixed-citation></ref><ref id="scirp.77630-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Bhardwaj, A. and Hartland, S. (1998) Studies on Buildup of Interfacial Film at the Crude Oil/Water Interface. 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