Relevant bibliographies by topics / Aspen Hysys and Modular Refinery

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  1. Journal articles
  2. Dissertations / Theses
  3. Conference papers

Academic literature on the topic 'Aspen Hysys and Modular Refinery'

Author: Grafiati
Published: 5 June 2025
Last updated: 2 August 2025

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Journal articles on the topic "Aspen Hysys and Modular Refinery"

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Michael, Adeloye Olalekan, Akpa Jackson Gonurubon, Dagde Kenneth Kekpugile, and Ehirim Emmanuel Odionyegbuechua. "Process Simulation and Performance Models for Enhanced Modular Refinery Operations in Nigeria." International Journal of Chemical Engineering and Applications 14, no. 1 (2023): 1–13. http://dx.doi.org/10.18178/ijcea.2023.14.1.798.

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The study aimed at availability of petroleum products in Nigeria through the operation of enhanced modular refinery process due to inefficient conventional major refineries. The enhanced modular refinery converts or processes residue product from conventional modular refinery as feedstock to the hydrocracker reactor for viable and desired products such as liquefied petroleum gas, naphtha and diesel. Therefore, twenty Nigerian crude oil types were classified as sweet, light and medium crude oil, and these crude oil types were categorized based on their recovery volume at true boiling point of 3
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Mamudu, Angela O., Goddy J. Igwe, Ebenezer Okonkwo, and Mohamed M. Rashad. "Process design evaluation of an optimum modular topping refinery for Nigeria crude oil using hysys® aspen software." Cogent Engineering 6, no. 1 (2019): 1659123. http://dx.doi.org/10.1080/23311916.2019.1659123.

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Makasheva, D. "Modeling and optimization of AVT-3 and AT-2 crude оil distillation units at Atyrau refinery". Herald of the Kazakh-British technical university 19, № 3 (2022): 15–22. http://dx.doi.org/10.55452/1998-6688-2022-19-3-15-22.

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The article shows examples of the use of Aspen Hysys software for optimization of the AVT-3 and AT-2 crude oil distillation units at Atyrau Oil Refinery. The Aspen Hysys software was implemented at the Atyrau Refinery for the first time.Calculations were carried out to optimize AVT-3 and AT-2 crude distillation units of the Atyrau refinery with the construction of a model in Aspen Hysys. As a result of the calculations, the possibility of improving the efficiency of individual parts of units was revealed, pilot runs on the units were carried out to confirm. During the pilot run on the AVT-3 un
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Mohammed, Ayoob I., Thaer A. Abdulla, and Atta O. Hussein. "Steady State Simulation and Analysis of Crude Distillation Unit at Baiji Refinery." Journal of Petroleum Research and Studies 14, no. 1 (2024): 131–53. http://dx.doi.org/10.52716/jprs.v14i1.767.

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Abstract In this research work, the main distillation column of Salahadin 1 refinery in Baiji Refineries is simulated and analyzed using Aspen HYSYS. Kirkuk, Basrah and Ajeel crudes are mixed together (with unknown mixing ratio) to create the feed stream of this unit. The determination of the blending ratio of these streams beside performance analysis of the system using actual plant data to increase the operating capacity are the main objectives of this research work. So, this work is very helpful to the refinery because it can be applicable to manage these blending ratios to obtain desired p
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Saud, Iltifat Hameed, Abdulrazzaq Saeed Abdullah, Akram A. Al-Asadi, and Basma Al Janabi. "Study and optimization of the factors affecting the crude oil distillation process using ASPEN HYSYS." EUREKA: Physics and Engineering, no. 6 (November 1, 2024): 31–41. http://dx.doi.org/10.21303/2461-4262.2024.003311.

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Crude oil distillation (CDU) is a crucial unit in refinery plants for producing various crude oil cuts, such as naphtha, kerosene, light gas oil, heavy gas oil, and Atm residue. This study used ASPEN HYSYS V11 software to examine the parameters that affect CDU efficiency in South Refinery Company /Iraq-Mishriff crude oil, like temperature, pressure, and flow rate. Optimization of these variables was applied to identify suiTable values for separation products. The study reveals that the increased mass flow rate of crude oil to CDU increases the flow rates of naphtha, kerosene, and HGO. The stud
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Nabgan, Walid, Tuan Amran Tuan Abdullah, Bahador Nabgan, et al. "A Simulation of Claus Process Via Aspen Hysys for Sulfur Recovery." Chemical Product and Process Modeling 11, no. 4 (2016): 273–78. http://dx.doi.org/10.1515/cppm-2016-0019.

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Abstract In refineries, due to the environmental pollutions, sulfur content in petroleum need be reduced. The incineration process is used for sulfur recovery system which is not friendly process to the environment and needs high temperature. This actual process exhaust high amount of SO2 from the incinerator stack to the environment. The Claus process is the best method to recover sulfur from acid gases that contain hydrogen sulfide. The particular reaction for sulfur removal from sour gas is hydrogen sulfide (H2S) sulfur dioxide (SO2) reformation (2H2S+O2=S2+2H2O). The aim of this study is t
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Michael, Anemka Nabula, Dagde Kenneth, and Ikenyiri Patience. "Design and simulation of sour water unit: A case study of port Harcourt refining company." Chemistry International 9, no. 2 (2023): 68–76. https://doi.org/10.5281/zenodo.8118142.

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The simulation of a 35.0m<sup>3</sup>/hr sour water plant model using aspen hysys process simulator was carried out using 3 different fluids; steam, kerosene and naphtha, respectively.&nbsp; The major equipment in the plant model are: 3-phase separator, heat exchanger and absorber tower.&nbsp; The results of the parameter obtained from aspen HYSYS were presented in terms of material balance, Energy balance, sizing and costing.&nbsp; The material balance result in terms of composition (mole fraction) obtained from the absorber outlet stream for treated water were constant for naphtha and kerose
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Oyedeko, K. F., O. D. Ogunjimi, and A. A. Adesina. "Investigation of Naphtha Hydrotreating (NHT) Unit Exergy Utilization: A Case Study of a Petrochemical Industry in A developing Country." European Journal of Energy Research 2, no. 3 (2022): 9–14. http://dx.doi.org/10.24018/ejenergy.2022.2.3.50.

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The need for efficient energy use in refinery operations is the proffered solution to the poor management of energy resources which has resulted in the instability in oil products prices, irregular plant shutdowns experienced in refineries of developing countries and increased carbon emission to the atmosphere. This research work aims to carry out exergy analysis on major energy consuming units which will aid in determining sites and causes of primary energy losses and proffer solutions to maximizing energy utilization. The Naphtha Hydro-treating (NHT) unit of the case model refinery was succe
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Jin, Qibing, Ziming Li, Zhicheng Yan, Bin Wang, and Zeyu Wang. "Optimization Study on Enhancing Deep-Cut Effect of the Vacuum Distillation Unit (VDU)." Processes 10, no. 2 (2022): 359. http://dx.doi.org/10.3390/pr10020359.

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The vacuum distillation unit (VDU) is the key unit to produce vacuum gas oil and vacuum residue, which has a very important impact on the downstream secondary processing units. The optimization of deep-cut vacuum distillation seeks to improve the yield of heavy vacuum gas oil (HVGO) and its dry point temperature, which is related to the economic benefits of the refinery. In this study, we first established a simple model of a VDU by using the Aspen HYSYS Process simulation software. Then, we built a rigorous model with fast convergence by using the initial values obtained by the simple model.
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Oliveira, H. D. Z. S., Y. C. Santiago, A. M. González, I. F. Pinheiro, K. P. Barbosa, and L. A. Sphaier. "OIL SLUDGE THERMOCHEMICAL CONVERSION: GASIFICATION AND AMMONIA SYNTHESIS CASE." Brazilian Journal of Petroleum and Gas 17, no. 2-3 (2023): 63–73. http://dx.doi.org/10.5419/bjpg2023-0004.

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This work aims to evaluate the gasification of oily sludge (OS) and the potential use of produced gas as feedstock for ammonia production. For this purpose, a computational gasification model was developed and validated in Aspen Hysys® v. 11.0 software to evaluate the influence of air/steam mixtures as gasification agents on the studied parameters. The Lower Heating Value (LHV) of the producer gas varied between 5 and 10 MJ/m3 for equivalence ratios greater than 0.3. The molar concentration of H2 increased to 24.9% at 1380°C and decreased to 21.5% at 1700°C. Finally, the producer gas was used
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Dissertations / Theses on the topic "Aspen Hysys and Modular Refinery"

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Ordouei, Mohammad Hossein. "Computer Aided Simulation and Process Design of a Hydrogenation Plant Using Aspen HYSYS 2006." Thesis, 2009. http://hdl.handle.net/10012/4431.

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Nowadays, computers are extensively used in engineering modeling and simulation fields in many different ways, one of which is in chemical engineering. Simulation and modeling of a chemical process plant and the sizing of the equipment with the assistance of computers, is of special interests to process engineers and investors. This is due to the ability of high speed computers, which make millions of mathematical calculations in less than a second associated with the new powerful software that make the engineering calculations more reliable and precise by making very fast iterations in thermo
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Conference papers on the topic "Aspen Hysys and Modular Refinery"

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Okwonna, O. O., A. A. Obuebite, and I. I. Osedebamen. "Optimization of AGO and DPK Production in an Industrial Modular Refinery Operation." In SPE Nigeria Annual International Conference and Exhibition. SPE, 2024. http://dx.doi.org/10.2118/221792-ms.

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Abstract Optimization of automotive gas oil (AGO) and dual-purpose kerosene (DPK) production in an industrial modular refinery operation was conducted using a case study of a facility (Company A) located at Ohaji-Egbema Local Government Area, Imo State, Nigeria. The system was modelled using the Aspen HYSYS version 11.0 simulation tool. A daily input of 5,000 barrels of crude oil per day was characterized and introduced into the distillation system operating at 101.3 kPa. The distillation column consisted of 22 trays for the collection of five target products: Off-gas, Naphtha, DPK, AGO and re
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Nešic, S., S. Fominykh, A. Vertlyugina, A. Sizykh, and U. Božovic. "Decarbonization Challenges in Oil Refining: A Perspective on Blue Hydrogen Production at Panchevo Oil Refinery." In SPE Europe Energy Conference and Exhibition. SPE, 2024. http://dx.doi.org/10.2118/220018-ms.

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Abstract The paper aims to outline the technical challenges and opportunities associated with implementing blue hydrogen production in the Panchevo oil refinery. It will emphasize a viable pathway for decarbonization, focusing on optimizing carbon capture and storage technologies, ensuring cost-effectiveness, and addressing environmental concerns. The scope includes contributing to the refinery's sustainability goals and fostering innovation in the energy transition. The approach involves utilizing Aspen Hysys for CO2 emission calculations, assessing all refinery emitters, and defining the car
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MUHAMMAD, Nabil Fikri bin Shariffuddin. "Quantification and mitigation of carbon footprint in petroleum refinery process through simulation software." In Decarbonization Technology: ICDT2024. Materials Research Forum LLC, 2025. https://doi.org/10.21741/9781644903575-41.

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Abstract. Petroleum refineries play a crucial role in producing various petroleum products through processes such as distillation, redistillation, cracking, and reforming. As the second-largest consumer of energy among industries, petroleum refineries significantly contribute to GHG emissions, particularly through combustion-related sources like process heaters and boilers. Therefore, it is crucial to adopt sustainable approaches to control and reduce these emissions. Simulation software like Aspen Plus/Symmetry can be utilized to quantify greenhouse gas emissions in petroleum refineries. This
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Mamudu, O. A., G. J. Igwe, and E. Okonkwo. "Process Design Evaluation of an Optimum Modular Topping Refinery for Nigeria Crude Oil Using HYSYS Software." In SPE Nigeria Annual International Conference and Exhibition. Society of Petroleum Engineers, 2016. http://dx.doi.org/10.2118/184342-ms.

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Ndunagu, Paschal Uzoma, Emeka Emmanuel Alaike, and Theophile Megueptchie. "A Practical Approach to Energy Optimization Using Pinch Analysis: A Case Study of an Oil Refinery." In SPE Nigeria Annual International Conference and Exhibition. SPE, 2021. http://dx.doi.org/10.2118/207096-ms.

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Abstract The objective of this paper is to perform an energy optimization study using pinch analysis on the Heat Exchanger Network (HEN) of a Crude Distillation Unit to maximum heat recovery, minimize energy consumption and increase refining margin. The heat exchanger network (HEN) considered comprises exchangers from the pre-heat section of the atmospheric distillation unit, which recovers heat from the product streams to incrementally heat the crude oil feed stream before entering the furnace. This paper illustrates how to perform a detailed HEN retrofitting study using an established design
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Jolaoso, Lateef A., Javad Asadi, Chuancheng Duan, and Pejman Kazempoor. "A Novel Hydrogen Economy Based on Electrochemical Cells Fully Integrated With Fossil Fuel Assets and Wastewater Resources." In ASME 2022 16th International Conference on Energy Sustainability collocated with the ASME 2022 Heat Transfer Summer Conference. American Society of Mechanical Engineers, 2022. http://dx.doi.org/10.1115/es2022-80238.

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Abstract Water and energy are two inseparable and interdependent phenomena that play essential roles in economic productivity and sustainable development. This paper presents a novel, highly efficient, and modular hydrogen production unit that can be fully integrated with numerous power production units, including coal and natural gas-fired power plants. The system is designed to utilize various water sources as the process’s feedstock. All process components, including waste-water treatment system, flue gas cooling, separating unit, and high-temperature solid oxide electrolyzer cell (SOEC), a
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