<?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">ANP</journal-id><journal-title-group><journal-title>Advances in Nanoparticles</journal-title></journal-title-group><issn pub-type="epub">2169-0510</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/anp.2023.121001</article-id><article-id pub-id-type="publisher-id">ANP-122789</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Biomedical&amp;Life Sciences</subject><subject> Chemistry&amp;Materials Science</subject><subject> Engineering</subject></subj-group></article-categories><title-group><article-title>
 
 
  Investigation of Physical Properties of Nano Crude Petroleum: Increasing Oil Flow Rate in Reservoirs
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Haniyeh</surname><given-names>Zare</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Mehdi</surname><given-names>Bosaghzadeh</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Frshad</surname><given-names>Farahbod</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>Department of Chemical Engineering, Esfarayen University of Technology, Esfarayen, Iran</addr-line></aff><aff id="aff2"><addr-line>Department of Chemical Engineering, Firoozabad Branch, Islamic Azad University, Firoozabad, Iran</addr-line></aff><pub-date pub-type="epub"><day>01</day><month>02</month><year>2023</year></pub-date><volume>12</volume><issue>01</issue><fpage>1</fpage><lpage>10</lpage><history><date date-type="received"><day>8,</day>	<month>December</month>	<year>2022</year></date><date date-type="rev-recd"><day>30,</day>	<month>January</month>	<year>2023</year>	</date><date date-type="accepted"><day>2,</day>	<month>February</month>	<year>2023</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>
 
 
  The zinc oxide nano-particles have been used in this research. In this work, zinc oxide nanoparticles have been added to light and heavy crude oil. In this research, thermoelectric and physical properties of light and heavy crude petroleum have been measured, experimentally. In addition, dimensionless groups in hydrodynamics and heat transfer calculations are presented. This research illustrates that heat capacity of light and heavy crude petroleum varies from 4256 J/kg&#183;&#176;C to 4457 J/kg&#183;&#176;C and 4476 J/kg&#183;&#176;C to 5002 J/kg&#183;&#176;C, respectively. Moreover, heat capacity of light and heavy nano-crude petroleum is changing from about 4285 J/kg&#183;&#176;C to 4496 J/kg&#183;&#176;C and 4494 J/kg&#183;&#176;C to 5021 J/kg&#183;&#176;C, respectively.
 
</p></abstract><kwd-group><kwd>Crude Petroleum</kwd><kwd> Thermoelectric</kwd><kwd> Kinetic Properties</kwd><kwd> Nano-Metals</kwd><kwd> Dimensional Numbers</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Today, energy is considered as one of the most basic human needs. Energy is a vital need for industry, food production and agricultural production [<xref ref-type="bibr" rid="scirp.122789-ref1">1</xref>]. This is despite the fact that a large percentage of the world’s energy is provided by fossil fuels, the use of which inevitably causes harm to human health, and damages to equipment and the facilities of various industries that use them follow [<xref ref-type="bibr" rid="scirp.122789-ref2">2</xref>]. The fossil fuels are divided into three main types including coal, oil and natural gas. All of three categories began to form a few hundred thousand years ago [<xref ref-type="bibr" rid="scirp.122789-ref3">3</xref>]. Before the appearance of dinosaurs, the period when these fuels began to form is called the “Carboniferous” period, which is a part of the Paleozoic era. “Carboniferous” takes its name from carbon, which is the most important component of coal and other fossil fuels [<xref ref-type="bibr" rid="scirp.122789-ref4">4</xref>]. The reason why they are called fossil fuels is that at that time the earth was full of swamps that were covered with huge trees and ferns and other leafy plants, and as the trees and plants died, they sank into the depths of the oceans and were gradually buried and layered [<xref ref-type="bibr" rid="scirp.122789-ref5">5</xref>]. Finally, a sponge called peat was formed [<xref ref-type="bibr" rid="scirp.122789-ref6">6</xref>]. After hundreds of years, peat was covered with sand, clay, and other minerals, and these minerals turned into a kind of sedimentary rock over time [<xref ref-type="bibr" rid="scirp.122789-ref7">7</xref>]. As more layers are piled up, they weigh more [<xref ref-type="bibr" rid="scirp.122789-ref8">8</xref>]. These types of fossil fuels have been used at different times and according to the level of technical knowledge and human ability to explore, exploit and use them in daily life, work and industry [<xref ref-type="bibr" rid="scirp.122789-ref9">9</xref>]. But it is obvious that nowadays the use of oil and gas is much more and more extensive than coal [<xref ref-type="bibr" rid="scirp.122789-ref10">10</xref>]. Oil is another fossil fuel that was formed more than three hundred million years ago [<xref ref-type="bibr" rid="scirp.122789-ref11">11</xref>]. Some scientists believe that the origin of oil is aquatic organisms, each of which is the size of a needle tip, and they can act just like plants [<xref ref-type="bibr" rid="scirp.122789-ref12">12</xref>]. Finally absorb sunlight and convert the energy stored in themselves. These tiny organisms fall to the bottom of the sea after death and are gradually buried under sedimentary layers and rocks, and the rocks and rocks put pressure on these tiny organisms, and the energy in their bodies cannot be discharged, and the carbon over time, under extreme heat and pressure, it turns into oil [<xref ref-type="bibr" rid="scirp.122789-ref13">13</xref>]. The need for oil has been a major factor in many of the wars of the twentieth century, including World War II. The United Arab Emirates, Saudi Arabia and the United States are the top three oil producers. In recent years, the development and advancement of micro-technologies has led to the manufacture and equipment’s production on a micro and nano scale that is used in various industries [<xref ref-type="bibr" rid="scirp.122789-ref14">14</xref>]. The use of nano-metals as a surface enhancer can also improve the performance of cooling and heating systems. Hence fluid flow theory is often well established. While the fully developed slow current is still theoretically achieved, a current with other properties, such as turbulent flow, must rely on laboratory and experimental relationships. It should be noted that all the fluid flow in the pipe has a zero velocity profile in the pipe wall, due to the non-slip condition to the maximum in the center of the pipe. Some research studies the dynamic properties of oil. Some others examine the thermodynamic properties of oil [<xref ref-type="bibr" rid="scirp.122789-ref15">15</xref>]. Also, other researches refer to the investigation of electrical properties of crude oil [<xref ref-type="bibr" rid="scirp.122789-ref16">16</xref>]. Other studies investigate the thermal properties and heat transfer mechanisms of oil passing through the pipeline [<xref ref-type="bibr" rid="scirp.122789-ref17">17</xref>]. However, no study has investigated the thermoelectric and kinetic properties of crude oil mixed with nanoparticles. Therefore, this research is significantly different from other researches. In this research, nanotechnology has been used to investigate the thermoelectric properties of high and low density oils.</p></sec><sec id="s2"><title>2. Materials and Method</title><sec id="s2_1"><title>2.1. API Grade of Crude Petroleum</title><p>The feed stream is two types of light and heavy crude oil. The American standard grade of crude petroleum is according to <xref ref-type="table" rid="table1">Table 1</xref>.</p></sec><sec id="s2_2"><title>2.2. Properties of ZnO</title><p>The nano-ZnO have been used in this work due to high value of the specific surface. In addition, the ZnO nano particle is a non-toxic in low concentrations. The data show a good relationship between health and appropriate concentrations of ZnO compounds (<xref ref-type="table" rid="table2">Table 2</xref>).</p></sec><sec id="s2_3"><title>2.3. Production of Nano-ZnO</title><p>The ZnO is used to make a solution 1 molar of Zn<sup>2+</sup>. At the first, Zn<sup>2+</sup> solution is purified, then a type of 0.05 M active surfactant, as well as 10% ethanol, is mixed with the Zn<sup>2+</sup> solution in ultrasonic. The produced solution is shaken at regular intervals. Then, the same reactants are mixed with a molar solution of sodium carbonate under similar conditions. Two produced solutions are mixed, proportionally. The reconstituted solution is shaken under ultrasonic conditions for half an hour. Then, another active surfactant is added to the obtained solution and mixed again for half an hour. The final solution is filtered and rinsed several times with pure water and ethanol under ultrasonic conditions, alternately.</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Composition of crude petroleum</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Composition</th><th align="center" valign="middle" >Crude petroleum grade</th></tr></thead><tr><td align="center" valign="middle" >Heavy crude petroleum</td><td align="center" valign="middle" >26.2</td></tr><tr><td align="center" valign="middle" >Light crude petroleum</td><td align="center" valign="middle" >49.1</td></tr></tbody></table></table-wrap><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Physical properties of ZnO</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Characteristics</th><th align="center" valign="middle" >ZnO</th></tr></thead><tr><td align="center" valign="middle" >Grid parameters in 300 K</td><td align="center" valign="middle" ></td></tr><tr><td align="center" valign="middle" >—a<sub>0</sub> nm</td><td align="center" valign="middle" >0.31563</td></tr><tr><td align="center" valign="middle" >—c<sub>0</sub> nm</td><td align="center" valign="middle" >0.51763</td></tr><tr><td align="center" valign="middle" >—c<sub>0</sub>/a<sub>0</sub></td><td align="center" valign="middle" >1.71</td></tr><tr><td align="center" valign="middle" >Density (grams per cubic centimeter)</td><td align="center" valign="middle" >5.632</td></tr><tr><td align="center" valign="middle" >Stable phase at 300 degrees K</td><td align="center" valign="middle" >Wurtzite</td></tr><tr><td align="center" valign="middle" >melting point (˚C)</td><td align="center" valign="middle" >1975</td></tr><tr><td align="center" valign="middle" >Thermal conductivity (W/m&#183;K)</td><td align="center" valign="middle" >1.14</td></tr><tr><td align="center" valign="middle" >Static dielectric constant</td><td align="center" valign="middle" >656/8</td></tr><tr><td align="center" valign="middle" >Refractive index</td><td align="center" valign="middle" >2.006</td></tr><tr><td align="center" valign="middle" >Exciton binding energy (mV)</td><td align="center" valign="middle" >58</td></tr><tr><td align="center" valign="middle" >Effective mass of electrons</td><td align="center" valign="middle" >0.27</td></tr></tbody></table></table-wrap></sec><sec id="s2_4"><title>2.4. Laboratory Equipment</title><p>The laboratory equipment includes a mixer tank, adiabatic test tube, and electric heater, which has been used to investigate the thermoelectric behavior of light and heavy petroleum. At the first, the crude petroleum is mixed with nano-ZnO in an ultrasonic (400 W and 180 min). Then, nano-oil is mixed in a mixing tank and then passed through an electric heater until the temperature reaches to 30˚C to 84˚C.</p></sec></sec><sec id="s3"><title>3. Results and Discussion</title><sec id="s3_1"><title>3.1. Effect of Nano-ZnO on Oil Density</title><p>The effect of adding zinc nano oxide on the density is illustrated in <xref ref-type="fig" rid="fig1">Figure 1</xref>. Increasing the percentage of nano-ZnO increases oil density.</p><p>Changes in the percentages of nano-ZnO from 1% to 5% increase density from 8 lb/gallon to 8.34 lb/gallon for light oil and also from 8.9 lb/gallon to 9.36 lb/gallon for heavy nano-crude petroleum. The experimental results show that average increase in density with addition of nano-ZnO is about 9.6%.</p></sec><sec id="s3_2"><title>3.2. Viscosity of Nano-Oil</title><p><xref ref-type="fig" rid="fig2">Figure 2</xref> illustrates the dynamic viscosity versus shear rate. Increasing shear rate reduces dynamic viscosity for both types of oil.</p><p>The experiments show that increasing shear rate reduces dynamic viscosity about 28%. In addition, decrease in the dynamic viscosity may be related to the interaction between oil and nano-ZnO.</p></sec><sec id="s3_3"><title>3.3. Initial Tension of Nano-Oil</title><p>The initial tension change is 1.1 Pa to 2 Pa for light nano-crude oil and 1.7 Pa to 2.9 Pa for heavy nano-crude oil (<xref ref-type="fig" rid="fig3">Figure 3</xref>). Two experimental relationships are expressed to predict initial tension in terms of temperature. The regression of the relationships is close to one. Hence, the accuracy of the curves is very good.</p><p>The relationship between initial tension and nano-ZnO is illustrated in <xref ref-type="fig" rid="fig4">Figure 4</xref>.</p></sec><sec id="s3_4"><title>3.4. Prandtl Number of Heavy and Light Nano-Oil</title><p>The change in Prandtl number in terms of percentage of nano-ZnO is illustrated in <xref ref-type="fig" rid="fig5">Figure 5</xref>. The results show that the trend of both curves is decreasing and can be predicted by logarithmic function.</p></sec><sec id="s3_5"><title>3.5. Investigation of Thermal Conductivity and Thermal Diffusivity</title><p>The change in the thermal conductivity ratio of light and heavy nano-oil versus percentage of nano-ZnO is illustrated in <xref ref-type="fig" rid="fig6">Figure 6</xref>. The experimental data show that thermal conductivity ratio is greater than one. It means that the ratio of thermal conductivity for light and heavy nano-oil is improved. This ratio is 0.1 to 1.15 for light nano-oil and 1.09 to 1.21 for heavy nano-oil. Results illustrate average difference between values of two curves is 5.2%, approximately.</p><p><xref ref-type="fig" rid="fig7">Figure 7</xref> illustrates the effect of nano-ZnO on the thermal conductivity with temperature change. In this experiment, the percentage of nano-ZnO varies from 1% to 5%. The studies show that increasing percentage of nano-ZnO usually increases the energy transfer capacity of materials. Therefore, it increases thermal conductivity from 0.15 W/m<sup>2</sup>∙K to 0.164 W/m<sup>2</sup>∙K for light nano-oil and 0.165 W/m<sup>2</sup>∙K to 0.182 W/m<sup>2</sup>∙K for heavy nano-oil. The studies show that the use of nano-ZnO increases thermal conductivity about 9%.</p></sec><sec id="s3_6"><title>3.6. Thermal Diffusivity of Heavy and Light Nano-Oil</title><p>The thermal diffusivity ratios for light and heavy nano-oil are 1.07 to 1.25 and 1.03 to 1.16, respectively. The experimental results show that thermal diffusivity ratio in 1% to 2% by volume of nano-ZnO is increasing sharply and this ratio in 2% to 5% by volume of nano-ZnO is almost constant. <xref ref-type="fig" rid="fig8">Figure 8</xref> illustrates relationship between thermal diffusivity ratio and percentage of nano-ZnO.</p><p><xref ref-type="fig" rid="fig9">Figure 9</xref> illustrate effect of percentage of nano-ZnO on thermal diffusivity. An increasing has been obtained for both nano-crude petroleum samples. This behavior is predictable according to the definition of the quantity of thermal diffusivity. The results show that changes of percentage of nano-ZO have a positive effect on thermal conductivity and a negative effect on density and heat capacity. Therefore, increasing nano-ZnO has a positive effect on thermal diffusivity.</p></sec><sec id="s3_7"><title>3.7. Study of Overall Heat Transfer Coefficient</title><p>The overall heat transfer coefficient is measured in <xref ref-type="fig" rid="fig1">Figure 1</xref>0. The regression of curves of light nano-oil and heavy nano-oil is 0.9056 and 0.9248, respectively. Operational data show that the kinetic ability of oil molecules increases with increasing nano-ZnO.</p></sec></sec><sec id="s4"><title>4. Conclusion</title><p>In this work, important thermoelectric and physical properties of light and heavy nano-petroleum have been measured. In addition, dimensionless groups in hydrodynamics and heat transfer calculations are presented. The effect of operating conditions and nano-ZnO on physical thermal properties of crude oil has been investigated. Results show that the heat capacity of light and heavy crude petroleum varies from 4256 J/kg∙˚C to 4457 J/kg∙˚C and 4476 J/kg∙˚C to 5002 J/kg∙˚C, respectively. Moreover, the heat capacity of light and heavy nano-crude petroleums is changing from 4285 J/kg∙˚C to 4496 J/kg∙˚C and 4494 J/kg∙˚C to 5021 J/kg∙˚C, respectively. Experimental results show that the ratio of thermal diffusion increases when the percentage of nanoparticles added to oil is equal to one to two and is almost constant at higher percentages. This study shows that increasing percentage of nano-ZnO increases energy transfer capacity. Therefore, it increases the thermal conductivity from 0.15 W/m<sup>2</sup>∙K to 0.164 W/m<sup>2</sup>∙K for light nano-crude oil and 0.165 W/m<sup>2</sup>∙K to 0.182 W/m<sup>2</sup>∙K for heavy nano-crude oil. Experiments show that increasing shear rate reduces dynamic viscosity about 28%.</p></sec><sec id="s5"><title>Conflicts of Interest</title><p>The authors declare no conflicts of interest regarding the publication of this paper.</p></sec><sec id="s6"><title>Cite this paper</title><p>Zare, H., Bosaghzadeh, M. and Farahbod, F. (2023) Investigation of Physical Properties of Nano Crude Petroleum: Increasing Oil Flow Rate in Reservoirs. Advances in Nanoparticles, 12, 1-10. https://doi.org/10.4236/anp.2020.121001</p></sec></body><back><ref-list><title>References</title><ref id="scirp.122789-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Zhou, C.H., Wang, Y.Y., Huang, X.T., et al. (2020) Optimization of Ultrasonic-Assisted Oxidative Desulfurization of Gasoline and Crude Petroleum. Chemical Engineering and Processing—Process Intensification, 147, Article ID: 107789. https://doi.org/10.1016/j.cep.2019.107789</mixed-citation></ref><ref id="scirp.122789-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Qin, J.S., Peng, X., Qiu, Q.P. and Tang, C. (2022) A New Type of Nano APTES-hBN Modified Palm Oil as Natural Ester Insulating Oil with Upgraded Thermal Aging Characteristics. 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