<?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">OJMSi</journal-id><journal-title-group><journal-title>Open Journal of Modelling and Simulation</journal-title></journal-title-group><issn pub-type="epub">2327-4018</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/ojmsi.2022.104020</article-id><article-id pub-id-type="publisher-id">OJMSi-120386</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Physics&amp;Mathematics</subject></subj-group></article-categories><title-group><article-title>
 
 
  30,000 bpd Capacity Modified Modular Refinery Operations in Nigeria
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Adeloye</surname><given-names>Olalekan Michael</given-names></name><xref ref-type="aff" rid="aff1"><sub>1</sub></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib></contrib-group><aff id="aff1"><label>1</label><addr-line>Department of Chemical/Petrochemical Engineering, Rivers State University, Port Harcourt, Nigeria</addr-line></aff><pub-date pub-type="epub"><day>24</day><month>08</month><year>2022</year></pub-date><volume>10</volume><issue>04</issue><fpage>340</fpage><lpage>348</lpage><history><date date-type="received"><day>23,</day>	<month>May</month>	<year>2022</year></date><date date-type="rev-recd"><day>10,</day>	<month>October</month>	<year>2022</year>	</date><date date-type="accepted"><day>13,</day>	<month>October</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>
 
 
  The study investigated and classified twenty Nigerian crude oil types based on their products recovery volume at true boiling point temperature of 370&amp;#730C using crude oil assay analysis data into Group A (crude oil with recovery volume above 80%), Group B (crude oil with recovery volume between 70% and 79%) and Group C (crude oil with recovery volume below 70%) respectively. Thus, twenty Nigerian crude oil types were simulated in a modified modular refinery (modified topping plant) of 30,000
   
  bpd capacity and twenty-nine (29) column trays number using Aspen Hysys software. Furthermore, the residues from the conventional modular refinery were processed as feedstock or precursor into the hydrocracker reactor attached to the stripping section of the modified modular refinery to yield more valuable products of liquefied petroleum gas, naphtha, diesel and bottom (residue). The simulation results of the modified modular refinery w
  ere
   compared with conventional modular refinery in terms of their residual yield percentage as Nigerian Brass 2012 of API 40.62, recovery volume 88.78%, yielded residue of 11.22% and 1.29% for conventional modular and modified modular refineries respectively while Okoro 2012 of least API 23.54, recovery volume 57.84%, yielded residue of 42.16% and 4.92% for conventional modular and modified modular refineries respectively. Thus, the residual or bottom product issue associated with operational process of conventional modular refinery operations in Nigeria due to inefficient or non-operational conventional major refinery in Nigeria has been resolved to minimum or least amount with the operational process of modified modular refinery operations in Nigeria.
 
</p></abstract><kwd-group><kwd>Modified Modular Refinery</kwd><kwd> Hydrocracker</kwd><kwd> Topping Plant Residue</kwd><kwd> Simulation</kwd><kwd> Aspen Hysys</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Crude oil refining involves subjecting the feedstock to a series of physical and chemical processes as a result of which different products are generated. The amount of reserve from the petroleum reservoir, together with oil and gas prices, operating costs and taxes controls the cash flow of the industry [<xref ref-type="bibr" rid="scirp.120386-ref1">1</xref>]. Petroleum refining processes are chemical engineering processes and other facilities used in crude oil refineries (also referred to as oil refineries) to transform crude oil into useful products such as liquefied petroleum gas, gasoline, kerosene, jet fuel, diesel oil and fuel oils [<xref ref-type="bibr" rid="scirp.120386-ref2">2</xref>]. Crude oil refineries are very large industrial complexes that involve many different processing units and auxiliary facilities such as utility units and storage tanks. Each refinery has its own unique arrangement and combination of refining processes largely determined by the refinery location, desired products and economic considerations [<xref ref-type="bibr" rid="scirp.120386-ref3">3</xref>]. In many ways, oil refineries technology is similar to a chemical plant and crude oil feedstock is processed in oil production plant before refining. There is usually an oil depot (tank farm) at or near an oil refinery for the storage of incoming crude oil feedstock as well as bulk liquid products, and oil refinery is considered an essential part of the downstream sector of the petroleum industry [<xref ref-type="bibr" rid="scirp.120386-ref4">4</xref>]. Raw or unprocessed crude oil is not generally useful in industrial applications, although light, sweet crude oil (low viscosity, low sulphur) has been used directly as a burner fuel to produce steam for the propulsion of seagoing vessels [<xref ref-type="bibr" rid="scirp.120386-ref5">5</xref>]. The lighter elements, however, form explosive vapours in the fuel tanks and are therefore hazardous, especially in warships. Thus, the different hydrocarbon molecules in crude oil are separated in a refinery operation into components that can be used as fuels, lubricants, and as feedstocks in petrochemical processes that manufacture products such as plastics, detergents, solvents, elastomers and fibers (nylon and polyesters) [<xref ref-type="bibr" rid="scirp.120386-ref6">6</xref>].</p><p>Oil refineries are large-scale plants, processing about a hundred thousand to several hundred thousand barrels of crude oil per day. Due to this high capacity, many of the units operate continuously as opposed to processing in batches, at steady state or nearly steady state for months to years. The high capacity also makes process optimization and advanced process control very desirable [<xref ref-type="bibr" rid="scirp.120386-ref7">7</xref>]. Once crude oil is extracted from the ground, it is transported and refined into petroleum products that have different values. These products are then transported to end-use consumers or retailers. The overall well-to-consumer supply chain for petroleum products is often described as being segmented into three components [<xref ref-type="bibr" rid="scirp.120386-ref8">8</xref>].</p><p>1) Upstream Activities:This involves exploring for crude oil deposits and the production of crude oil. Examples of firms that would belong in the upstream segment of the industry include companies that own rights to drill for oil such as ExxonMobil and companies that provide support services to the drilling segment of the industry such as Halliburton [<xref ref-type="bibr" rid="scirp.120386-ref9">9</xref>].</p><p>2) Midstream Activities:This involves the distribution of crude oil to refiners, the refining of crude oil into saleable products and the distribution of products to wholesalers and retailers. Examples of firms that would belong in the midstream segment of the industry include companies that transport oil by pipeline, truck or barge such as Oando Plc and companies that refine crude oil such as the Nigerian National Petroleum Corporation [<xref ref-type="bibr" rid="scirp.120386-ref9">9</xref>].</p><p>3) Downstream Activities: This involves the retail sale of petroleum products. Gasoline stations commonly referred as filling or petrol stations in Nigeria are perhaps the most visible downstream companies, but companies that deliver heating oil or propane would also fall into this category [<xref ref-type="bibr" rid="scirp.120386-ref9">9</xref>].</p><p>Crude oil is essentially a mixture of many different hydrocarbons, all of varying compositions and complexities. In order to separate the crude oil into different components that make up the raw natural resource, crude oil must be refined (refinery process) so that components can be removed according to their temperature difference (Boiling points) [<xref ref-type="bibr" rid="scirp.120386-ref10">10</xref>]. Thus, the Nigeria government owns and operates four major refineries through the Nigerian National Petroleum Corporation (NNPC) namely, old and new Port-Harcourt Refining Company (OPHRC and NPHRC), Kaduna Refining and Petrochemical Company Limited (KRPC) and Warri Refining and Petrochemical Company Limited (WRPC). Despite these refineries, 80% of petroleum products consumed in Nigeria are based on importation as the refineries operate less than 20% to 25% of its original capacities [<xref ref-type="bibr" rid="scirp.120386-ref9">9</xref>] [<xref ref-type="bibr" rid="scirp.120386-ref11">11</xref>] [<xref ref-type="bibr" rid="scirp.120386-ref12">12</xref>]. Therefore, the dependency on importation of petroleum products in Africa’s largest crude oil producer, Nigeria has led to incessant and continual scarcity of petroleum products. In addition, illegal refineries that feed on stolen crude oil abound in Nigeria with its associated operational and production hazards such as environmental pollution, crude oil theft, fire safety risk and poor quality petroleum products etc [<xref ref-type="bibr" rid="scirp.120386-ref13">13</xref>]. To curb the incessant and continual scarcity of petroleum products, environmental hazard associated with illegal (local) refineries, and reducing to minimal the importation of petroleum products, the existing refineries must be revamped and operated at full capacity, while new refineries are built by partnering with private sector thereby leading to deregulation of the sector [<xref ref-type="bibr" rid="scirp.120386-ref14">14</xref>]. Since construction of major refineries are capital intensive and time consuming, modular refineries have been licensed as a panacea to scarcity of petroleum products to meet local demands in Nigeria, thereby enhancing the availability of good quality products by eliminating illegal refineries and its associated environmental hazards.</p><p>A modular refinery can be built and operational within fourteen months of contract execution, thereby providing valuable fuels for host communities for vehicles, power generation, water treatment, and employment chances [<xref ref-type="bibr" rid="scirp.120386-ref10">10</xref>] The components of modular refinery include tankage, a distillation unit, facilities for gas recovery, and light hydrocarbons, and utility systems such as steam, power, and water-treatment plants. Topping refineries yield large amounts of unprocessed product (residue) and local markets determines its installation. The modular refinery process gives high quality control level, effective application of space and pre-delivery testing for efficient process functionality. Its available capacities ranges between 1000 and 30,000 barrels per day (bpd) [<xref ref-type="bibr" rid="scirp.120386-ref15">15</xref>] Topping refineries are hastily becoming a viable, flexible and cost effective scheme for petroleum producers especially where there is quick requirement to meet local need of crude oil products with relatively low investment cost, speed and construction period are some of the major advantages of a modular refinery [<xref ref-type="bibr" rid="scirp.120386-ref16">16</xref>] However, conventional modular refinery (topping plant) have been reported with associated issue of bottom product (residue) as my researches are silent with this stripping section residue or product [<xref ref-type="bibr" rid="scirp.120386-ref10">10</xref>] [<xref ref-type="bibr" rid="scirp.120386-ref12">12</xref>] [<xref ref-type="bibr" rid="scirp.120386-ref17">17</xref>] [<xref ref-type="bibr" rid="scirp.120386-ref18">18</xref>] [<xref ref-type="bibr" rid="scirp.120386-ref19">19</xref>] [<xref ref-type="bibr" rid="scirp.120386-ref20">20</xref>]. Therefore, pipeline networks and tankers are proposed or used in developed countries for transporting topping plant stripping section residue to conventional major refinery for further processing into more valuable end products. However, these are not obtainable in Nigeria due to the topography and inefficient operational condition of the conventional major refineries. Hence, this research study focused on improving valuable petroleum products yield from conventional modular refinery operations in Nigeria through the processing of the stripping section product (residue) of the conventional modular refinery as feedstock to hydrocracker reactor attached to the stripping section of the conventional modular (topping plant) refinery. In addition, the hydrocracker reactor is a catalytic hydrogenation process that applied nickel catalyst in converting atmospheric residue to more valuable desired products. The hydrocracking operation is enhanced as the required hydrogen gas is produced via steam-methane process since methane is the first product from the conventional or modified modular refinery. Thus, the modified modular refinery yielded more valuable petroleum finished products such as liquefied petroleum gas (which are required for domestic and heating purposes in Nigeria), naphtha (a useful precursor for petrochemical industry) and diesel (highly needed for automobile vehicle and also source of electricity supply to homes and industries due to low availability of electric power supply in Nigeria) in addition to the initial products from conventional modular refinery operations in Nigeria.</p></sec><sec id="s2"><title>2. Materials and Method</title><p>The materials applied in this research study include twenty (20) different types of Nigerian crude oil, API values, modified modular refinery, residue, Aspen Hysys Version 10 etc. Therefore, the following procedures are applied in performing this research study.</p><sec id="s2_1"><title>2.1. Crude Oil Classification</title><p>Twenty (20) Nigeria crude oil types were classified using Aspen Hysys software based on crude oil assay analysis and products recovery volume percentage at 370˚C and the results shown in Tables 1-3 respectively.</p></sec><sec id="s2_2"><title>2.2. Modified Modular Refinery Process</title><p>Twenty-Nine (29) column trays number were applied in a modified modular refinery in which hydrocracker was attached to its stripping section as shown.</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Group A nigerian crude oil with over 80% recovery volume</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Crude Oil Type</th><th align="center" valign="middle" >Recovery Volume (%)</th><th align="center" valign="middle" >Residue (%)</th></tr></thead><tr><td align="center" valign="middle" >Nigerian Brass 2012</td><td align="center" valign="middle" >88.78</td><td align="center" valign="middle" >11.22</td></tr><tr><td align="center" valign="middle" >Brass River 2011</td><td align="center" valign="middle" >88.65</td><td align="center" valign="middle" >11.35</td></tr><tr><td align="center" valign="middle" >Oso Condensate 2016</td><td align="center" valign="middle" >88.17</td><td align="center" valign="middle" >11.83</td></tr><tr><td align="center" valign="middle" >Agbami 2012</td><td align="center" valign="middle" >87.91</td><td align="center" valign="middle" >12.09</td></tr><tr><td align="center" valign="middle" >Erha 2012</td><td align="center" valign="middle" >83.66</td><td align="center" valign="middle" >16.34</td></tr><tr><td align="center" valign="middle" >Akpo 2014</td><td align="center" valign="middle" >83.41</td><td align="center" valign="middle" >16.59</td></tr><tr><td align="center" valign="middle" >Akpo Blend 2011</td><td align="center" valign="middle" >82.84</td><td align="center" valign="middle" >17.16</td></tr><tr><td align="center" valign="middle" >Forcados Blend 2014</td><td align="center" valign="middle" >81.49</td><td align="center" valign="middle" >18.51</td></tr></tbody></table></table-wrap><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Group B nigerian crude with recovery volume between 70% and 79%</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Crude Oil Types</th><th align="center" valign="middle" >Recovery Volume (%)</th><th align="center" valign="middle" >Residue (%)</th></tr></thead><tr><td align="center" valign="middle" >Nigerian Brass 2015</td><td align="center" valign="middle" >76.25</td><td align="center" valign="middle" >23.75</td></tr><tr><td align="center" valign="middle" >Okwori 2011</td><td align="center" valign="middle" >75.62</td><td align="center" valign="middle" >24.38</td></tr><tr><td align="center" valign="middle" >Amenam Blend 2011</td><td align="center" valign="middle" >74.56</td><td align="center" valign="middle" >25.44</td></tr><tr><td align="center" valign="middle" >Bonny Light 2011</td><td align="center" valign="middle" >73.19</td><td align="center" valign="middle" >26.81</td></tr><tr><td align="center" valign="middle" >Qua Iboe 2012</td><td align="center" valign="middle" >72.55</td><td align="center" valign="middle" >27.45</td></tr><tr><td align="center" valign="middle" >Okwuibome 2014</td><td align="center" valign="middle" >72.04</td><td align="center" valign="middle" >27.96</td></tr></tbody></table></table-wrap><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> Group C nigerian crude oil with recovery volume below 70%</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Crude Oil Type</th><th align="center" valign="middle" >Recovery Volume (%)</th><th align="center" valign="middle" >Residue</th></tr></thead><tr><td align="center" valign="middle" >Nigerian Forcados 2012</td><td align="center" valign="middle" >69.70</td><td align="center" valign="middle" >30.30</td></tr><tr><td align="center" valign="middle" >Bonga 2012</td><td align="center" valign="middle" >68.53</td><td align="center" valign="middle" >31.47</td></tr><tr><td align="center" valign="middle" >Bonga 2014</td><td align="center" valign="middle" >67.55</td><td align="center" valign="middle" >32.45</td></tr><tr><td align="center" valign="middle" >Usan 2013</td><td align="center" valign="middle" >66.34</td><td align="center" valign="middle" >33.66</td></tr><tr><td align="center" valign="middle" >Usan 2015</td><td align="center" valign="middle" >63.81</td><td align="center" valign="middle" >36.19</td></tr><tr><td align="center" valign="middle" >Okoro 2012</td><td align="center" valign="middle" >57.84</td><td align="center" valign="middle" >42.16</td></tr></tbody></table></table-wrap><p>Hence, the twenty (20) crude oil types were simulated in a modified modular refinery at operating temperature of 370˚C to yield product components as off gas, naphtha, kerosene, diesel, atmospheric gas oil and residue. In optimizing or enhancing production from conventional modular refinery, the residue was further processed as feedstock to hydrocracker reactor of the modified modular refinery in a catalytic hydrogenation process. Thus, the feedstock is processed in the hydrocracker reactor in the presence of nickel supported catalyst at operating conditions of 380˚C and 183 bar respectively, and hydrogen gas is produced and introduced into the hydrocracker reactor via steam-methane reforming process. The steam-methane reforming process is applied in this study for the hydrogen gas production as methane, which is the first light product of</p><p>both conventional and modified modular refinery is the main feedstock or precursor for the process. Hence, more valuable products produced via the hydrocracker process are liquefied petroleum gas (LPG), which is cooled and stored at temperature below −42˚C (−43.6˚F), naphtha, diesel and bottom. Thus, the simulation processes were carried out for crude oil on the basis of 30,000 barrel per day (902.1Kgmol/hr) (<xref ref-type="fig" rid="fig1">Figure 1</xref>).</p></sec></sec><sec id="s3"><title>3. Result and Discussion</title><p>The results of this research study are discussed thus.</p><sec id="s3_1"><title>3.1. Crude Oil Classification</title><p>The results of the crude oil classification on twenty (20) Nigerian crude oil types using Aspen Hysys comprises of the crude oil assay results and their products recovery volume percent at true boiling point of 370˚C. Thus, the twenty (20) Nigerian crude oil types were classified into three groups namely: Group A, Group B and Group C as shown in Tables 1-3 respectively. Therefore, Group A Nigerian crude oil types yielded high recovery volume of eighty percent (80%) and above and relatively low sulphur contents. Also, Nigerian crude oil types with recovery volume percent between 70 and 79 are categorised as Group B as shown in <xref ref-type="table" rid="table2">Table 2</xref>, while Nigerian crude oil type with recovery volume less than seventy (70%) are categorized as Group C as posited in <xref ref-type="table" rid="table3">Table 3</xref></p></sec><sec id="s3_2"><title>3.2. Modified Modular Refinery Simulation</title><p>The simulation process results of the twenty (20) Nigerian crude oil types in a modified modular refinery were compared with the simulation results of conventional modular refinery as presented by Adeloye, 2022 as highlighted in <xref ref-type="table" rid="table4">Table 4</xref>. Thus, <xref ref-type="table" rid="table4">Table 4</xref> showed the residual percentages of the twenty crude oil types from conventional modular refinery and modified modular refinery simulation process respectively. It can be deduced that there is huge reduction in residual percentages of individual crude oil type when subjected to conventional and modified modular refineries respectively.</p><p>Hence, Okoro 2012 with the least API value among the twenty crude oil types yielded residual percent of 42.16 and 4.92 in conventional and modified modular refinery respectively</p><table-wrap id="table4" ><label><xref ref-type="table" rid="table4">Table 4</xref></label><caption><title> Residual product percent of modular and modified modular refinery</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Crude Oil Type</th><th align="center" valign="middle"  colspan="2"  >Residue (%)</th></tr></thead><tr><td align="center" valign="middle" >Modular Refinery</td><td align="center" valign="middle" >Modified Modular Rrefinery</td></tr><tr><td align="center" valign="middle" >Nigerian Brass 2012</td><td align="center" valign="middle" >11.22</td><td align="center" valign="middle" >1.29</td></tr><tr><td align="center" valign="middle" >Brass River 2011</td><td align="center" valign="middle" >11.35</td><td align="center" valign="middle" >1.30</td></tr><tr><td align="center" valign="middle" >Oso Condensate 2016</td><td align="center" valign="middle" >11.83</td><td align="center" valign="middle" >1.27</td></tr><tr><td align="center" valign="middle" >Agbami 2012</td><td align="center" valign="middle" >12.09</td><td align="center" valign="middle" >1.39</td></tr><tr><td align="center" valign="middle" >Erha 2012</td><td align="center" valign="middle" >16.34</td><td align="center" valign="middle" >1.85</td></tr><tr><td align="center" valign="middle" >Akpo 2014</td><td align="center" valign="middle" >16.59</td><td align="center" valign="middle" >1.77</td></tr><tr><td align="center" valign="middle" >Akpo Blend 2011</td><td align="center" valign="middle" >17.16</td><td align="center" valign="middle" >1.84</td></tr><tr><td align="center" valign="middle" >Forcados Blend 2014</td><td align="center" valign="middle" >18.51</td><td align="center" valign="middle" >2.15</td></tr><tr><td align="center" valign="middle" >Nigerian Brass 2015</td><td align="center" valign="middle" >23.75</td><td align="center" valign="middle" >2.71</td></tr><tr><td align="center" valign="middle" >Okwori 2011</td><td align="center" valign="middle" >24.38</td><td align="center" valign="middle" >2.62</td></tr><tr><td align="center" valign="middle" >Amenam Blend 2011</td><td align="center" valign="middle" >25.44</td><td align="center" valign="middle" >2.54</td></tr><tr><td align="center" valign="middle" >Bonny Light 2011</td><td align="center" valign="middle" >26.81</td><td align="center" valign="middle" >3.08</td></tr><tr><td align="center" valign="middle" >Qua Iboe 2012</td><td align="center" valign="middle" >27.45</td><td align="center" valign="middle" >3.14</td></tr><tr><td align="center" valign="middle" >Okwuibome 2014</td><td align="center" valign="middle" >27.96</td><td align="center" valign="middle" >3.22</td></tr><tr><td align="center" valign="middle" >Nigerian Forcados</td><td align="center" valign="middle" >30.30</td><td align="center" valign="middle" >3.54</td></tr><tr><td align="center" valign="middle" >Bonga 2012</td><td align="center" valign="middle" >31.47</td><td align="center" valign="middle" >3.66</td></tr><tr><td align="center" valign="middle" >Bonga 2014</td><td align="center" valign="middle" >32.45</td><td align="center" valign="middle" >3.78</td></tr><tr><td align="center" valign="middle" >Usan 2013</td><td align="center" valign="middle" >33.66</td><td align="center" valign="middle" >3.95</td></tr><tr><td align="center" valign="middle" >Usan 2015</td><td align="center" valign="middle" >36.19</td><td align="center" valign="middle" >4.22</td></tr><tr><td align="center" valign="middle" >Okoro 2012</td><td align="center" valign="middle" >42.16</td><td align="center" valign="middle" >4.92</td></tr></tbody></table></table-wrap></sec></sec><sec id="s4"><title>4. Conclusion</title><p>Twenty (20) Nigerian crude oil types were analysed and classified for modified modular refinery operations as panacea to resolve the residue or bottom issue associated with conventional modular refinery in Nigeria. The resulting residues of these crude oil types were processed as feedstock in a hydrocracker reactor attached to the conventional modular refinery stripping section to yield more valuable products such as liquefied petroleum gas, naphtha, diesel and bottom. Thus, the modified modular refinery yielded a very low residual percentage volume in comparison to the conventional modular refinery, thereby resolving the residue or bottom product issue associated with conventional modular refinery operations in Nigeria due to inefficient operational level of conventional major refinery in Nigeria. Thus, the study recommends the naphtha product as precursor or feedstock for petrochemical operation while the bottom product of the hydrocracker reactor can be utilized as feedstock for further refining operational process for recovery of more useful and valuable products.</p></sec><sec id="s5"><title>Conflicts of Interest</title><p>The author declares no conflicts of interest regarding the publication of this paper.</p></sec><sec id="s6"><title>Cite this paper</title><p>Michael, A.O. (2022) 30,000 bpd Capacity Modified Modular Refinery Operations in Nigeria. Open Journal of Modelling and Simulation, 10, 340-348. https://doi.org/10.4236/ojmsi.2022.104020</p></sec></body><back><ref-list><title>References</title><ref id="scirp.120386-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Adeloye, O.M., Abu, K.U. and Abu, R.N. (2015) Quantifying Uncertainty in Oil Reserve Estimate. Research Journal of Engineering Sciences, 4, 1-8.</mixed-citation></ref><ref id="scirp.120386-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Colwell, R.F. (2009) Oil Refinery Processes: A Brief Overview. Process Engineering Associate Publisher, Tennessee.</mixed-citation></ref><ref id="scirp.120386-ref3"><label>3</label><mixed-citation publication-type="other" xlink:type="simple">James, G.S. (2014) The Chemistry and Technology of Petroleum. CRC Press, Boca Raton.</mixed-citation></ref><ref id="scirp.120386-ref4"><label>4</label><mixed-citation publication-type="other" xlink:type="simple">Brian, B. (2000) Petrolia: The Landscape of America’s First Oil Boom. Johns Hopkins University Press, Baltimore.</mixed-citation></ref><ref id="scirp.120386-ref5"><label>5</label><mixed-citation publication-type="other" xlink:type="simple">Feng, L., Hu, Y., Hall, C.A.S. and Wang, J. (2013) The Chinese Oil Industry: History and Future. Springer-Verlag Publisher, New York.</mixed-citation></ref><ref id="scirp.120386-ref6"><label>6</label><mixed-citation publication-type="other" xlink:type="simple">Gary, J.H. and Handwerk, G.E. (2001) Petroleum Refining Technology and Economics. Marcel Dekker Incorporated, New York.</mixed-citation></ref><ref id="scirp.120386-ref7"><label>7</label><mixed-citation publication-type="other" xlink:type="simple">Spataru, C. (2017) Whole Energy System Dynamics: Theory, Modelling and Policy. Routledge, London. https://doi.org/10.4324/9781315755809</mixed-citation></ref><ref id="scirp.120386-ref8"><label>8</label><mixed-citation publication-type="other" xlink:type="simple">Leone, J. and Leone, W. (2014) The Process of Crude Oil Refining. Department of Energy and Mineral Engineering, Pennstate College of Earth and Mineral Science, State College. https://www.e-education.psu.edu/eme801/node/470</mixed-citation></ref><ref id="scirp.120386-ref9"><label>9</label><mixed-citation publication-type="other" xlink:type="simple">Adeloye, O.M., Cyrus, A. and Afolayan, J.T. (2022) Analysis and Classification of Nigerian Crude Oil Types for Modular Refinery Operations. SSRG International Journal of Chemical Engineering Research, 9, 17-24. https://doi.org/10.14445/23945370/IJCER-V9I2P104</mixed-citation></ref><ref id="scirp.120386-ref10"><label>10</label><mixed-citation publication-type="other" xlink:type="simple">Bello, S.K., Lamidi, S.B. and Bello, K.A. (2020) A Review of Sustainable Modular Refineries Development in Nigeria: Prospects and Challenges. Global Scientific Journal, 8, 1230-1240.</mixed-citation></ref><ref id="scirp.120386-ref11"><label>11</label><mixed-citation publication-type="other" xlink:type="simple">Ogbuigwe, A. (2018) Refining in Nigeria: History, Challenges and Prospects. Applied Petrochemical Research, 8, 181-192. https://doi.org/10.1007/s13203-018-0211-z</mixed-citation></ref><ref id="scirp.120386-ref12"><label>12</label><mixed-citation publication-type="other" xlink:type="simple">Nwaozuzu, C. (2014) Crude Oil Refining in Africa and the Way Forward. Energy Mix Report.</mixed-citation></ref><ref id="scirp.120386-ref13"><label>13</label><mixed-citation publication-type="other" xlink:type="simple">Nigerian Society of Chemical Engineers (NSChE) (2017) The Modular Refinery Strategy. The Nigerian Society of Chemical Engineers Newsletter, Lagos, 12-14.</mixed-citation></ref><ref id="scirp.120386-ref14"><label>14</label><mixed-citation publication-type="other" xlink:type="simple">Iheukwumere, O.E., Moore, D. and Omotayo, T. (2020) Investigating the Challenges of Refinery Construction in Nigeria: A Snapshot across Two-Time Frames over the Past 55 Years. International Journal of Construction Supply Chain Management, 10, 46-72.</mixed-citation></ref><ref id="scirp.120386-ref15"><label>15</label><mixed-citation publication-type="other" xlink:type="simple">Brickstone (2018) Modular Refinery Project Development and Financing: Nigeria. Key Development Considerations. Brickstone Africa Research. https://reports.brickstone.africa/whitepapers/WHP-MODULAR-REFINERY</mixed-citation></ref><ref id="scirp.120386-ref16"><label>16</label><mixed-citation publication-type="other" xlink:type="simple">Idris, M.N., Zubaira, A., Baba, D. and Adamu, M.N. (2018) Design and Development of 15,000Barrel per day Capacity of Modular Crude Oil Refinery Plant. International Journal of Engineering and Modern Technology, 2, 1-8.</mixed-citation></ref><ref id="scirp.120386-ref17"><label>17</label><mixed-citation publication-type="other" xlink:type="simple">Mamudu, A.O., Igwe, G.J. and Okonkwo, E. (2019) Process Design Evaluation of an Optimum Modular Topping Refinery for Nigeria Crude Oil Using Aspen Hysys Software. Cogent Engineering, 6, Article ID: 1659123. https://doi.org/10.1080/23311916.2019.1659123</mixed-citation></ref><ref id="scirp.120386-ref18"><label>18</label><mixed-citation publication-type="other" xlink:type="simple">Mamudu, A., Okoro, E., Igwilo, K., Olabode, O., Elehinafe, F. and Odunlami, O. (2019) Challenges and Prospects of Converting NigeriaIllegal Refineries to Modular Refineries. The Open Chemical Engineering Journal, 13, 1-6. https://doi.org/10.2174/1874123101913010001</mixed-citation></ref><ref id="scirp.120386-ref19"><label>19</label><mixed-citation publication-type="other" xlink:type="simple">Ogbon, N.M., Otanocha, O. and Rim-Rukeh, A. (2018) An Assessment of the Economic Viability and Competitiveness of Modular Refinery in Nigeria. Nigerian Journal of Technology, 37, 1015-1025. https://doi.org/10.4314/njt.v37i4.22</mixed-citation></ref><ref id="scirp.120386-ref20"><label>20</label><mixed-citation publication-type="other" xlink:type="simple">Adeloye, O.M. (2022) Process Simulation and Models for Enhanced Modular Refinery Operations in Nigeria. Ph.D. Thesis, Faculty of Engineering, Rivers State University, Port Harcourt.</mixed-citation></ref></ref-list></back></article>