<?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">ACES</journal-id><journal-title-group><journal-title>Advances in Chemical Engineering and Science</journal-title></journal-title-group><issn pub-type="epub">2160-0392</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/aces.2022.121002</article-id><article-id pub-id-type="publisher-id">ACES-114479</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Chemistry&amp;Materials Science</subject></subj-group></article-categories><title-group><article-title>
 
 
  Effect of Cassava Starch and Sodium Carbonate on the Properties of Local Drilling Mud: Beneficiation to Improve the Rheological and Flow Properties of Locally Formulated Mud
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Andrew</surname><given-names>Odeh</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>Redemption</surname><given-names>Edegbe</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>Eghe</surname><given-names>Oyedoh</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>Department of Chemical Engineering, Faculty of Engineering, University of Benin, Benin, Nigeria</addr-line></aff><pub-date pub-type="epub"><day>09</day><month>12</month><year>2021</year></pub-date><volume>12</volume><issue>01</issue><fpage>13</fpage><lpage>25</lpage><history><date date-type="received"><day>27,</day>	<month>October</month>	<year>2021</year></date><date date-type="rev-recd"><day>4,</day>	<month>January</month>	<year>2022</year>	</date><date date-type="accepted"><day>7,</day>	<month>January</month>	<year>2022</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>
 
 
  Drilling mud is a key component in drilling operations and in accessing oil and gas reservoirs. Bentonite is applied as a viscosifier, fluid loss control agent, and as a weighting material in water-based drilling mud. The type of bentonite used in drilling mud formulation is sodium bentonite due to its high dispersion properties and high swelling capacity. Nigeria has a huge bentonite clay deposit resources which can be evaluated and enhanced in order to be utilized as drilling mud. However, bentonite clay from different parts of Nigeria was investigated and found to be calcium bentonite which is not suitable for drilling mud, because it has low swelling capacity and poor rheological properties. In this study, local bentonite obtained from Afuze, Edo state was used to formulate different samples of drilling mud with each treated using thermo-chemical beneficiation process with sodium carbonate and cassava starch, and then undergo characterization to identify the changes in physical properties and finally, draw comparison with API values for standard drilling mud. The results obtained from this study indicates that, the flow and rheological properties of the beneficiated drilling mud developed through thermo-chemical treatment, showed significant improvement compared to the untreated mud. Therefore, pure calcium bentonite from natural deposits in Nigeria can be modified to sodium bentonite and sufficiently used in drilling mud formulation.
 
</p></abstract><kwd-group><kwd>Drilling Mud</kwd><kwd> Bentonite Clay</kwd><kwd> Beneficiation</kwd><kwd> Cassava Starch</kwd><kwd> Rheological Properties</kwd><kwd> Characterization</kwd><kwd> Oil and Gas Reservoir</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>As one of the largest oil producers in the world, the present consumption of bentonite clay in the drilling operations in Nigeria alone is over 100 thousand tons a year [<xref ref-type="bibr" rid="scirp.114479-ref1">1</xref>]. This large consumption has led to various attempts in finding a local substitute which can save a huge amount of hard currency that otherwise would be spent on importation [<xref ref-type="bibr" rid="scirp.114479-ref2">2</xref>].</p><p>Drilling muds, oil or water-based, are made up of clays, water, weighing materials and chemical additives used to flush cuttings from the drill bit to the surface. The most common type of clay used in drilling mud formation is the bentonite clay. Bentonite clay is deposited in millions of tons across various locations in Nigeria which includes but not restricted to; Edo, Delta, Imo, Yobe, Borno and Kebbi States [<xref ref-type="bibr" rid="scirp.114479-ref3">3</xref>]. The properties and formulation of drilling fluids play a fundamental role in drilling operations [<xref ref-type="bibr" rid="scirp.114479-ref4">4</xref>]. Since the success of drilling operations depends on the correct selection of the drilling fluid system [<xref ref-type="bibr" rid="scirp.114479-ref5">5</xref>], most of the bentonite used in the Nigerian mud formulation is imported to avoid disasters associated with the use of inferior quality bentonite. The under-utilization of the Nigerian bentonite clay is predominantly due to its major constituent. It has been found that Nigeria bentonite has defects in fluid loss and rheological properties (including yield point). In addition, due to the high calcium content and low sodium content compared with foreign bentonite, it does not meet the API drilling standards. Due to these or more difficulties, Nigeria’s bentonite used in drilling activities is mainly imported into the country [<xref ref-type="bibr" rid="scirp.114479-ref6">6</xref>]. A lot of studies and researches have been focused on characterizing and beneficiating our local clay to the American Petroleum Institute (API) standard [<xref ref-type="bibr" rid="scirp.114479-ref7">7</xref>]. Although Nigerian bentonite has a large number of mineral deposits all over the country, it has not been widely used due to its excessive water loss and low swelling index [<xref ref-type="bibr" rid="scirp.114479-ref8">8</xref>].</p><p>In terms of foreign exchange, the Nigerian economy is highly dependent on the oil and gas industry. Over the years, researchers have confirmed that drilling activities carried out by oil companies require the import of materials required for fluid formulations or the import of custom drilling fluids specifically designed to meet the needs of the formation of the Niger Delta [<xref ref-type="bibr" rid="scirp.114479-ref9">9</xref>]. The costs associated with importing these materials can reach millions of dollars each year, affecting the nation’s gross domestic product (GDP) and eventually the economy [<xref ref-type="bibr" rid="scirp.114479-ref10">10</xref>]. Importing bentonite for drilling in the oil and gas industry continues to change the huge amount of foreign exchange that can be used in Nigeria’s socio-economic stability budget [<xref ref-type="bibr" rid="scirp.114479-ref11">11</xref>]. Due to these or more difficulties, Nigeria’s bentonite used in drilling activities is mainly imported into the country [<xref ref-type="bibr" rid="scirp.114479-ref12">12</xref>]. Before this clay can be used to prepare drilling mud, sufficient measures have to be taken to modify it. It is also important and appropriate to enhance the properties of this clay. This particular demand has increased research on the use of local clays in drilling fluid applications in the oil and gas industry. As interest in bentonite usage in oil and gas industries increases, the properties of Nigerian bentonite need to be improved to meet API standards [<xref ref-type="bibr" rid="scirp.114479-ref13">13</xref>].</p><p>Cassava is one of the most abundant substances in nature with starch being its main constituent as about 25% starch may be obtained from mature, good quality tubers [<xref ref-type="bibr" rid="scirp.114479-ref14">14</xref>]. Ademiluyi et al. [<xref ref-type="bibr" rid="scirp.114479-ref1">1</xref>] investigated the use of local cassava starch instead of imported samples from the viscosity and fluid loss control of aqueous mud. Igbani et al. [<xref ref-type="bibr" rid="scirp.114479-ref8">8</xref>] also studied using cassava starch powder and found that it could improve the density of drilling fluids. The results from both studies indicated that the local cassava imported samples had similar or better filtration control properties, but the viscosity of the drilling fluid produced from the local starch was also lower than that of the imported type. Therefore, a thorough study of local cassava is needed, in order to study their properties and develop a slurry formulation which can perform the same function as the imported additives. This will reduce the cost of some of the expensive viscosifiers and fluid loss agents that are imported and will also create jobs. Hence, this study evaluates the performance of local cassava as a viscosity enhancer and demulsifier in water-based drilling mud.</p><p>Beneficiation is a process which involves the addition of chemical additives like sodium carbonate (Na<sub>2</sub>CO<sub>3</sub>), caustic soda (NaOH), potassium chloride (KCl), sodium carboxymethyl cellulose (CMC), barium sulphate (Ba<sub>2</sub>SO<sub>4</sub>), starch, etc. to the mud formulation to help in improving drilling mud properties such as; free swell volume (FSV), gel strength, yield point, weight, specific gravity, viscosity, fluid loss. These additives help minimize formation damage, maintain well integrity, reduce logging analysis problems, protect water-sensitive shale, reduce fluid loss in the protective formation, and reduce well washout for better results, lining and cementing work [<xref ref-type="bibr" rid="scirp.114479-ref15">15</xref>] [<xref ref-type="bibr" rid="scirp.114479-ref16">16</xref>].</p>Location of Study Area<p>Bentonite clay used in this study was obtained from Afuze town in owan east local government area of Edo State, Southeastern Nigeria (<xref ref-type="fig" rid="fig1">Figure 1</xref>). Its geographical coordinates are longitude 6.04254˚7'E latitude 6.96945˚N and elevation of 440 ft (134 meters) and this is 533 ft (162.5 meters) below average elevation of Nigeria.</p></sec><sec id="s2"><title>2. Materials and Methods</title><sec id="s2_1"><title>2.1. Equipment and Raw Materials</title><p><xref ref-type="table" rid="table1">Table 1</xref> shows the equipment used in this work.</p><p><xref ref-type="table" rid="table2">Table 2</xref> shows the equipment used in this work.</p></sec><sec id="s2_2"><title>2.2. Methodology</title><sec id="s2_2_1"><title>2.2.1. Cassava Starch Flour Preparation</title><p>The cassava root variety known as azaka was uprooted, peeled and cut into small sizes which were properly washed and grated into pulp mash/paste. The pulp mash was then placed into a porous cloth and squeezed to extract as much filtrate (containing water and suspended starch) as possible which was received in</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Details of equipment used</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Equipment</th><th align="center" valign="middle" >Function(s)/Use(s)</th></tr></thead><tr><td align="center" valign="middle" >Graduated measuring cylinder</td><td align="center" valign="middle" >Measurement of specific volumes of solution</td></tr><tr><td align="center" valign="middle" >Beaker</td><td align="center" valign="middle" >For transfer and supply of measured volumes of liquid</td></tr><tr><td align="center" valign="middle" >pH meter</td><td align="center" valign="middle" >For determining pH of solution</td></tr><tr><td align="center" valign="middle" >Sieve</td><td align="center" valign="middle" >For separating unwanted particles present in the crushed clay material</td></tr><tr><td align="center" valign="middle" >Electronic weighing balance</td><td align="center" valign="middle" >For determining mass in grams</td></tr><tr><td align="center" valign="middle" >Stop watch</td><td align="center" valign="middle" >For measuring precise time</td></tr><tr><td align="center" valign="middle" >Mechanical overhead stirrer</td><td align="center" valign="middle" >For mixing drilling fluids in preparation for laboratory test</td></tr><tr><td align="center" valign="middle" >Mortar</td><td align="center" valign="middle" >For crushing the bentonite clay into small particles</td></tr><tr><td align="center" valign="middle" >Masking tape</td><td align="center" valign="middle" >For labelling samples for proper identification</td></tr><tr><td align="center" valign="middle" >Magnetic stirrer</td><td align="center" valign="middle" >For obtaining homogeneous liquid mixtures</td></tr><tr><td align="center" valign="middle" >Spatula</td><td align="center" valign="middle" >For measuring solid, moving objects and scraping materials out of beaker</td></tr><tr><td align="center" valign="middle" >Tachometer</td><td align="center" valign="middle" >For measuring the rotation speed of the overhead stirrer</td></tr><tr><td align="center" valign="middle" >Viscometer</td><td align="center" valign="middle" >For determining the viscosity of the various mud samples</td></tr><tr><td align="center" valign="middle" >Mechanical grater</td><td align="center" valign="middle" >For grinding cassava to pulp mash</td></tr><tr><td align="center" valign="middle" >Electric thermo-regulated oven</td><td align="center" valign="middle" >For drying solid wet starch</td></tr></tbody></table></table-wrap><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Details of raw materials used</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >S/N</th><th align="center" valign="middle" >Raw material</th><th align="center" valign="middle" >Function(s)</th><th align="center" valign="middle" >Quantity</th></tr></thead><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >Bentonite clay</td><td align="center" valign="middle" >Viscosity and filtration control</td><td align="center" valign="middle" >20 - 40 g</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >Water</td><td align="center" valign="middle" >Base fluid</td><td align="center" valign="middle" >350 ml</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >Cassava Starch</td><td align="center" valign="middle" >Viscosifier and fluid loss reducer</td><td align="center" valign="middle" >10 g</td></tr><tr><td align="center" valign="middle" >4</td><td align="center" valign="middle" >Sodium carbonate (Na<sub>2</sub>CO<sub>3</sub>)</td><td align="center" valign="middle" >Reduction of calcium content via cation exchange process</td><td align="center" valign="middle" >3.3 - 6.7 g</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >Sodium hydroxide (NaOH)</td><td align="center" valign="middle" >regulate the pH and decrease corrosion</td><td align="center" valign="middle" >0.3 g</td></tr></tbody></table></table-wrap><p>a bowl. The filtrate obtained was allowed to settle under the influence of gravity for about 7 hours in order for the starch to concentrate at the bottom while the water was removed. The solid starch obtained was then placed in a flat pan and placed in the electric thermo-regulated oven for hours to remove the moisture content. The dried starch cake was then crushed and sieved to obtain fine particles and finally packaged.</p></sec><sec id="s2_2_2"><title>2.2.2. Bentonite Clay Preparation</title><p>The bentonite clay obtained from Afuze was dried under moderate conditions and was crushed by pounding in a mortar. Sieve analysis was carried out on the crushed clay with the use of a sieve shaker using different mesh sizes to obtain fine particles. Proportions of 20 g, 25 g, 30 g, 35 g and 40 g of fine bentonite clay were weighed and placed in different beakers labelled appropriately.</p></sec><sec id="s2_2_3"><title>2.2.3. Preparation of Sodium Carbonate Solution</title><p>Sodium carbonate solution formulated by dissolving sodium carbonate powder (soda ash) in distilled water. This solution served as a source of carbonate and sodium ions for an ion exchange process with Ca-bentonite, where the calcium can be precipitated as calcium bentonite [<xref ref-type="bibr" rid="scirp.114479-ref11">11</xref>].</p></sec><sec id="s2_2_4"><title>2.2.4. Preparation of the Drilling Mud</title><p>The experimental procedure involved the addition of a bentonite clay sample to a sodium carbonate aqueous solution to form a bentonite suspension, which was stirred continuously for 1 hour 60˚C at speed of 150 rpm determined using a tachometer to form sodium bentonite and calcium carbonate. The calcium based bentonite was therefore converted to sodium based bentonite by combining chemical (addition of sodium carbonate), mechanical (agitation), and thermal (heating) treatment procedures. The bentonite clay sample was treated with sodium carbonate making use of a sodium carbonate bentonite weight ratio of 1:5 by varying the sodium carbonate content and bentonite concentration. The sodium carbonate/bentonite weight ratios are as follows; 20 g of local bentonite (no sodium carbonate), 4 g of sodium carbonate to 20 g of local bentonite, 5 g of sodium carbonate to 25 g of local bentonite, 6.0 g of sodium carbonate to 30 g of local bentonite, 7 g of sodium carbonate to 35 g of local bentonite, 8 g of sodium carbonate to 40 g of local bentonite.</p><p>Upon the formation of bentonite suspension, the bentonite suspension was heated and stirred continuously with the aid of a magnetic stirrer and a magnetic stirrer hot plate. The different samples (sample 2 - 6) were subsequently treated with 10 g of cassava starch flour and other chemical additives such as sodium hydroxide and potassium chloride for another 15 mins to form a bentonite-starch suspension and to achieve a homogenous dispersion where the polymer chains are well confined by the clay particles.</p></sec><sec id="s2_2_5"><title>2.2.5. Optimization by Means of Characterization</title><p>The various mud samples were then characterized by determining the rheological properties of the mud which consist of; plastic viscosity, apparent viscosity, yield point, mud density, specific gravity, alkalinity, and fluid loss. These parameters (plastic/apparent viscosity and yield point) were recorded with a viscometer at dial readings of 600 and 300 rpm. Formula for determining some of the aforementioned properties are;</p><p>plastic viscosity ( cp ) = 60 0rpm reading − 300 rpm reading (1)</p><p>apparent viscosity ( cp ) = 600rpm 2 (2)</p><p>yield point ( lbs / 100 ft 2 ) = 300   rpm − plastic viscosity (3)</p><p>mud density ( ppg ) = measured mass of agiven mud sample volume of the sample (4)</p><p>where rpm is revolution per time (mins) and ppg is pounds per gallon.</p><p>The fluid loss was determined by using a filter paper attached to a measuring cylinder. Each sample was poured gradually into the set up and the volume of liquid lost from the mud is measured in the measuring cylinder.</p></sec></sec></sec><sec id="s3"><title>3. Results and Discussion</title><p><xref ref-type="table" rid="table3">Table 3</xref> gives comprehensive details of results obtained from this study. Hydrogen ion concentration, pH is a measure of the concentration of hydrogen ions in aqueous solution. If the water used in the preparation of a drilling mud is too hard or the pH value is not within the range of 8.5 - 9.5, then the mud will take a longer period to hydrate, or it might not hydrate fully. <xref ref-type="fig" rid="fig2">Figure 2</xref> shows a bar plot comparing the pH of the imported bentonite, local bentonite, and the five different samples. A critical look at the plot indicated an increase in the pH of the mud samples. This increase occurred as a result of the beneficiation of the mud samples by the addition of sodium carbonate (Na<sub>2</sub>CO<sub>3</sub>). Sodium carbonate is alkaline in nature, as it is a strong base. The higher the bentonite and sodium carbonate concentrations, the higher</p><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> Overall summary of experimental result</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Measured properties</th><th align="center" valign="middle" >20 g Imported bentonite</th><th align="center" valign="middle" >20 g Local bentonite</th><th align="center" valign="middle" >20 g local bentonite + 4 g Na<sub>2</sub>CO<sub>3</sub> + 10 g cassava starch</th><th align="center" valign="middle" >25 g local bentonite + 5 g Na<sub>2</sub>CO<sub>3</sub> + 10 g cassava starch</th><th align="center" valign="middle" >30 g local bentonite + 6 g Na<sub>2</sub>CO<sub>3</sub> + 10 g cassava starch</th><th align="center" valign="middle" >35 g local bentonite + 7 g Na<sub>2</sub>CO<sub>3</sub> + 10 g cassava starch</th><th align="center" valign="middle" >40 g local bentonite + 8 g Na<sub>2</sub>CO<sub>3</sub><sub> </sub>+ 10 g cassava starch</th></tr></thead><tr><td align="center" valign="middle" >pH</td><td align="center" valign="middle" >10.21</td><td align="center" valign="middle" >7.80</td><td align="center" valign="middle" >10.50</td><td align="center" valign="middle" >10.55</td><td align="center" valign="middle" >10.60</td><td align="center" valign="middle" >10.70</td><td align="center" valign="middle" >10.90</td></tr><tr><td align="center" valign="middle" >Specific gravity</td><td align="center" valign="middle" >1.025</td><td align="center" valign="middle" >1.04</td><td align="center" valign="middle" >1.06</td><td align="center" valign="middle" >1.06</td><td align="center" valign="middle" >1.075</td><td align="center" valign="middle" >1.092</td><td align="center" valign="middle" >1.118</td></tr><tr><td align="center" valign="middle" >Mud density (ppg)</td><td align="center" valign="middle" >8.55</td><td align="center" valign="middle" >8.68</td><td align="center" valign="middle" >8.84</td><td align="center" valign="middle" >8.84</td><td align="center" valign="middle" >8.97</td><td align="center" valign="middle" >9.11</td><td align="center" valign="middle" >9.33</td></tr><tr><td align="center" valign="middle" >Viscosity (cp), 600 rpm</td><td align="center" valign="middle" >40.00</td><td align="center" valign="middle" >20.70</td><td align="center" valign="middle" >26.50</td><td align="center" valign="middle" >32.50</td><td align="center" valign="middle" >34.00</td><td align="center" valign="middle" >36.00</td><td align="center" valign="middle" >38.10</td></tr><tr><td align="center" valign="middle" >Viscosity (cp), 300 rpm</td><td align="center" valign="middle" >28.00</td><td align="center" valign="middle" >17.00</td><td align="center" valign="middle" >22.60</td><td align="center" valign="middle" >27.90</td><td align="center" valign="middle" >29.80</td><td align="center" valign="middle" >31.00</td><td align="center" valign="middle" >32.60</td></tr><tr><td align="center" valign="middle" >Plastic viscosity (cp)</td><td align="center" valign="middle" >12.00</td><td align="center" valign="middle" >3.70</td><td align="center" valign="middle" >3.90</td><td align="center" valign="middle" >4.60</td><td align="center" valign="middle" >4.20</td><td align="center" valign="middle" >5.00</td><td align="center" valign="middle" >5.50</td></tr><tr><td align="center" valign="middle" >Apparent viscosity (cp)</td><td align="center" valign="middle" >20.00</td><td align="center" valign="middle" >10.35</td><td align="center" valign="middle" >13.25</td><td align="center" valign="middle" >16.25</td><td align="center" valign="middle" >17.00</td><td align="center" valign="middle" >18.00</td><td align="center" valign="middle" >19.05</td></tr><tr><td align="center" valign="middle" >Yield point (lb/100 ft<sup>2</sup>)</td><td align="center" valign="middle" >16.00</td><td align="center" valign="middle" >13.33</td><td align="center" valign="middle" >18.70</td><td align="center" valign="middle" >23.30</td><td align="center" valign="middle" >25.60</td><td align="center" valign="middle" >26.00</td><td align="center" valign="middle" >27.10</td></tr><tr><td align="center" valign="middle" >Fluid loss (ml) at 30 min</td><td align="center" valign="middle" >11.00</td><td align="center" valign="middle" >52.50</td><td align="center" valign="middle" >29.00</td><td align="center" valign="middle" >26.50</td><td align="center" valign="middle" >19.00</td><td align="center" valign="middle" >15.70</td><td align="center" valign="middle" >12.60</td></tr></tbody></table></table-wrap><p>the pH values of the mud samples. The conversion of calcium carbonate to sodium carbonate through ion exchange can also influence the pH of the mud samples.</p><p>Specific gravity defines the density or weight of fluid compared to the density of an equal volume of water at a specified temperature. <xref ref-type="fig" rid="fig3">Figure 3</xref> is a plot showing the comparison between the specific gravity of the imported bentonite, local bentonite, and the five samples. The different readings obtained were compared with the standard bentonite and it was observed that there was also an increase in the specific gravity of the different samples. The increase in the specific gravity of samples was influenced by the addition of cassava starch to the five samples at different masses of bentonite and sodium carbonate [<xref ref-type="bibr" rid="scirp.114479-ref17">17</xref>].</p><p>A high mud density manages the formation pressure and improves the stability of the well bore. <xref ref-type="fig" rid="fig4">Figure 4</xref> is a bar plot showing the comparison between the densities of the standard bentonite, local bentonite, and the five different test samples. The different dial readings were compared with that of the imported bentonite, and it was observed that there was a progressive rise in the densities of the mud samples. An increase in mud density was greatly influenced by adding cassava starch to the different samples. Increase in the volume of the bentonite resulted in a higher effect of cassava starch on the mud samples increasing the mud density of the samples.</p><p>Mud viscosity illustrates the amount of resistance of the fluid to shear stress. For the effectiveness of the fluid to be able to remove cuttings, the fluid has to have some viscosity [<xref ref-type="bibr" rid="scirp.114479-ref16">16</xref>]. The viscosity of the drilling fluid can be improved upon by treatment with additives such as starch. <xref ref-type="fig" rid="fig5">Figure 5</xref> shows the comparison between the viscosities at 300 rpm and 600 rpm of the imported bentonite, local bentonite, and the five different samples. From the chart, it was observed that there were generally poor values of viscosity of untreated local bentonite when compared with the standard mud sample. However, with beneficiation, there was an improvement in the viscosity of the treated mud samples when compared with the untreated local bentonite. Cassava starch is suitable for increasing viscosity of the clay suspension and stabilizing the clay suspension. The higher the bentonite concentration, the higher the starch effect on the viscosity of the mud samples. From the result, the most improved viscosity was observed in sample seven (40 g of bentonite + 6.7 g of Na<sub>2</sub>CO<sub>3</sub> + 10 g of starch) having the highest concentration of bentonite.</p><p>The resistance of the flow of fluids due to mechanical friction in the drilling mud such as the shape and size of solid, concentration of solid, viscosity of the fluid phase in the continuous phase is known as plastic viscosity. <xref ref-type="fig" rid="fig6">Figure 6</xref> below shows the comparison between the plastic and apparent viscosities of the standard bentonite, local bentonite, and the five different samples. The values used for the plot of plastic viscosity were obtained from the difference between measurements at 600 rpm and measurements at 300 rpm [<xref ref-type="bibr" rid="scirp.114479-ref18">18</xref>]. The plastic viscosity</p><p>was relatively low when compared with the standard, and no significant improvement was observed even with an increase in the concentration of Na<sub>2</sub>CO<sub>3</sub> and cassava starch.</p><p>The measure of the viscosity of a fluid at a given shear rate is known as apparent viscosity. Apparent viscosity is half of the 600 rpm dial value. The apparent viscosity values are dependent on the 600 rpm dial values. Therefore, the highest value at 600 rpm will yield the highest apparent viscosity. From the plot, sample seven (40 g of Local Bentonite Clay + 6.7 g of Na<sub>2</sub>CO<sub>3</sub> + 10 g of cassava starch) had the highest apparent viscosity value. An increased bentonite concentration led to increased apparent viscosity. Compared with the imported bentonite, the values increased progressively and there was significant improvement in apparent viscosity when beneficiated with Na<sub>2</sub>CO<sub>3</sub> and cassava starch.</p><p>The resistance of the initial fluid flow or the needed stress to move the fluid is known to be the yield point. The yield point shows the capacity of drilling mud to transport cuttings to the surface. The yield point calculated from the Bingham equation is less than the true yield stress, which is required to maintain flow [<xref ref-type="bibr" rid="scirp.114479-ref3">3</xref>]. <xref ref-type="fig" rid="fig7">Figure 7</xref> below shows the comparison between the yield point of the standard bentonite, local bentonite, and the five different samples. From the plot, the different yield point values were as the difference between the values of viscosity at 300 rpm and plastic viscosity. Since there was a significant improvement in the reading of viscosity at 300 rpm and a slight improvement in plastic viscosity, the yield point of the samples improved significantly when compared with the imported bentonite.</p><p><xref ref-type="fig" rid="fig8">Figure 8</xref> is a bar chart showing the comparison between the fluid loss of the imported bentonite, local bentonite, and the five different samples. The lower the fluid loss, the more suitable the drilling mud and vice versa. It was observed from the plot that the local bentonite exhibited a very high level of fluid loss when compared with the standard bentonite. But after beneficiation with increased volume of the local bentonite, there was a relative improvement in the fluid loss of the treated samples compared to the untreated local bentonite as the filtration loss of the treated samples reduced drastically compared to the untreated bentonite.</p><p>Sample seven (40 g of Local Bentonite Clay + 6.7 g of Na<sub>2</sub>CO<sub>3</sub> + 10 g of cassava starch) showed the greatest improvement in filtration loss. The presence of cassava starch in the samples helped to reduce filtrate loss as cassava starch is a fluid loss reducer.</p></sec><sec id="s4"><title>4. Conclusion</title><p>As interest in bentonite usage increases in oil and gas facilities in Nigeria and all over the world, it is necessary to improve the rheological properties of Nigeria’s bentonite to make it comply with international API standards. This is necessary to prevent the country from losing huge amounts of money from international oil companies operating in Nigeria in the name of importing high-quality drilling mud. In order to maximize the use of local bentonite for drilling applications, the use of calcium bentonite with sodium carbonate, tapioca starch and other suitable additives becomes important. The results of this study showed that the combination of local clay, cassava starch and Na<sub>2</sub>CO<sub>3</sub> through heat treatment and mechanical agitation procedures improved some of the rheological and flow properties of the mud samples. The gradual increase in the concentration of bentonite and Na<sub>2</sub>CO<sub>3</sub> also affected the viscosity and properties of the mud samples. The higher the sodium carbonate concentration, the higher the alkalinity (pH) of the mud sample. Compared to the API standard, the mud sample with the highest concentration of bentonite and sodium carbonate (40 g of local bentonite + 6.7 g of Na<sub>2</sub>CO<sub>3</sub> + 10 g of cassava starch) showed the highest flow and rheological properties after the treatment. This means that with higher concentrations of additives, the quality of the local bentonite can be improved to the standards required for drilling operations. In order to increase the viscosity of the local bentonite, further research is recommended to use other chemical additives to change the rheological properties of the mud with economic analysis in view.</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>Odeh, A., Edegbe, R. and Oyedoh, E. (2022) Effect of Cassava Starch and Sodium Carbonate on the Properties of Local Drilling Mud: Beneficiation to Improve the Rheological and Flow Properties of Locally Formulated Mud. Advances in Chemical Engineering and Science, 12, 13-25. https://doi.org/10.4236/aces.2022.121002</p></sec></body><back><ref-list><title>References</title><ref id="scirp.114479-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Ademiluyi, F.T., Harry, T.F., Joel, O.F. and Oduola, K. (2016) Performance Evaluation of Local Cassava Starches with Imported Starch for Drilling Fluid. American Journal of Engineering Research (AJER), 5, 111-120.</mixed-citation></ref><ref id="scirp.114479-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Afolabi, R.O., Efeovbokan, V. and Orodu, O. (2017) Properties and Application of Nigerian Bentonite Clay Deposits for Drilling Mud Formulation: Recent Advances and Future Prospects. 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