Relevant bibliographies by topics / Atmospheric Distillation column

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  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers

Academic literature on the topic 'Atmospheric Distillation column'

Author: Grafiati
Published: 5 June 2025
Last updated: 1 August 2025

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Journal articles on the topic "Atmospheric Distillation column"

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Girish, M. Deshmukh*, and C. Shende Anand. "Design of Atmospheric Petroleum Distillation Column." Archives of Chemistry and Chemical Engineering 3, no. 1 (2021): 1–10. https://doi.org/10.5281/zenodo.5783274.

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<strong>Abstract</strong> This work summarizes the design procedure for Atmospheric Distillation Column for petroleum oil. The design and operation of crude distillation unit are still done almost on exclusively on an empirical basis. This is because crude petroleum and its products are made of large number of hydro-carbons. The complex mixture due to large number of fractions, side stripper, and reflux made the work of improving energy efficiency into a tedious manner. This creates adversity in designing the distillation column. The varied products are distinguished by performing true boiling
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Achmad Faisal Faputri and Indah Agus Setiorini. "PERFORMANCE EVALUATION OF TRAYS IN ATMOSPHERIC FRACTIONATION COLUMN WITH SOUTH PALEMBANG DISTRICT (SPD) CRUDE OIL FEED." Jurnal Cakrawala Ilmiah 2, no. 7 (2023): 3133–48. http://dx.doi.org/10.53625/jcijurnalcakrawalailmiah.v2i7.5467.

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Distillation's role is to separate the components it separates based on the boiling point of each component to produce the desired product with the principle of evaporation, namely the evaporation of components. In the industrial world the role of fractional distillation is very important. This study aims to design a fractional distillation apparatus, to know the process and performance of the column and the theory of fractionation separation with the role of column support facilities. Using raw material in the form of 10 liters of SPD crude oil, the separation is divided into three fractions.
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Tong, Zheng Ming, Chao Li, Jia Lei Lu, and Kai Zhu. "Energy-Saving Characteristics of Benzene-Toluene Mixtures in Heat Pump Distillation Column." Advanced Materials Research 455-456 (January 2012): 630–34. http://dx.doi.org/10.4028/www.scientific.net/amr.455-456.630.

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China is a big industrial energy consuming country. The largest proportion of energy consuming is the operations of separation in chemical industry, and the energy consumption of the distillation is the highest in separation. Therefore, it is very important to research energy-saving issues of the process of distillation in today's circumstances of the energy shortage. This article describes the model of heat pump distillation column,and its characteristics, uses static simulation programs to simulate operating conditions in the atmospheric pressure for the benzene-toluene material system, and
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Fumuassuca, Diana S., Marcilio Dos Santos, and Antonio A. Chivanga Barros. "Pinch Analysis Applied to Atmospheric Distillation Column." Angolan Mineral, Oil & Gas Journal 1, no. 1 (2020): 11–15. http://dx.doi.org/10.47444/amogj.v1i1.6.

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To increase the efficiency of industrial processes, mainly in petroleum refineries, the strategies to energy optimization are being developed. Thus, there is a need to know the energy consumption analysis in term of loss level and to define the procedure to recovery that. The analyses involve the flow rate study, based on energy balances that define the best strategy to use the energy, with the installation of heat exchanger networks. With the use of this procedure, we can reduce the operational costs, associated with a reduction of the level energy consumption. The study developed here was re
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Patrascioiu, Cristian. "Modelling the Atmospheric Distillation Using the Unisim Design Simulator." MATEC Web of Conferences 290 (2019): 10006. http://dx.doi.org/10.1051/matecconf/201929010006.

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The process of atmospheric distillation represents the first oil processing process realized in refineries, with a particular impact, both in terms of production and energy. The modeling and simulation of the atmospheric distillation process is one of the tools used to reduce operating costs and increase the efficiency of the industrial plant. The paper aims at presenting research concerning the calculation of liquid-vapor equilibrium for petroleum products as well as an exhaustive analysis of an oil distillation column modeling. The paper is an indispensable didactic component in the mathemat
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Zbytovský, Jiří, Tomáš Sommer, Martin Zapletal, and Jiří Trejbal. "Comparison of various column packing materials efficiency for hydrocarbons and aqueous mixtures." Chemical & biochemical engineering quarterly 33, no. 2 (2019): 183–90. http://dx.doi.org/10.15255/cabeq.2018.1565.

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The efficiency of industrial column packings is commonly tested by standard hydrocarbon mixtures. However, a reduced efficiency value is often observed, particularly during distillation of aqueous mixtures. In this paper, distillation experiments with various binary mixtures were carried out on different column packings to evaluate relative separation efficiencies of mixtures for each packing material. Each of the binary mixtures, which comprised heptane–methylcyclohexane, ethanol–water, morpholine–water, and acetic acid–water, was distilled under atmospheric pressure and total reflux ratio on
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Raeva, V. M., and A. M. Dubrovsky. "Comparison of extractive distillation flowsheets for methanol–tetrahydrofuran–water mixtures." Fine Chemical Technologies 15, no. 3 (2020): 21–30. http://dx.doi.org/10.32362/2410-6593-2020-15-3-21-30.

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Objectives. Synthesis and comparative analysis of the extractive distillation flowsheets for aqueous mixtures of solvents utilized in pharmaceutical industries using the example of a methanol−tetrahydrofuran−water system with various compositions. The ternary system contains two minimally boiling azeotropes that exist in a vapor–liquid phase equilibrium. To evaluate the selective effect of glycerol, the phase equilibria of the methanol–tetrahydrofuran–water and methanol–tetrahydrofuran–water–glycerol systems at 101.32 kPa were studied.Methods. The calculations were carried out in the Aspen Plu
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Semenov, Alexander, Yuri Podkamennyi, Yuri Bebikhov, and Ilya Yakushev. "Saving the environment by automation of crude oil distillation in a rectification column." E3S Web of Conferences 371 (2023): 01093. http://dx.doi.org/10.1051/e3sconf/202337101093.

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The article shows the results of the development of an automated control system for the distillation of oil in a distillation column, which makes it possible to save the environment. In the theoretical part, the process of distillation of crude oil in a distillation column is described and its technological scheme is given for atmospheric distillation with a single evaporation of oil. In the calculation part, the heat and material balance of mass transfer in the rectification column has been analyzed. In the practical part, the problems of installing process control instruments, improving the
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Mamudu, Angela O., Ebenezer Okonkwo, Stephen I. Okocha, Emeka E. Okoro, Francis Elehinafe, and Kevin Igwilo. "The Design of an Integrated Crude Oil Distillation Column with Submerged Combustion Technology." Open Chemical Engineering Journal 13, no. 1 (2019): 7–22. http://dx.doi.org/10.2174/1874123101912010007.

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Objective: Generally, Petroleum refineries are put in place to convert or refine unprocessed crude oil into more useful products using both physical separation and chemical conversion processes. Albeit, different refining unit are subsets of the physical separation category. The atmospheric and vacuum distillation unit seems to be more prominent. Conventionally, the crude atmospheric residue cannot be further heated in an atmospheric condition due to: coke formation, pipes plugging, thermal cracking and straining of the furnace. A vacuum distillation column is therefore required. Methods: This
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Jamali, M. A., A. Bissenbay, and N. Nuraje. "Thermodynamic Modeling and Process Simulation of Kumkol Crude Oil Refining." Eurasian Chemico-Technological Journal 25, no. 3 (2023): 183–92. http://dx.doi.org/10.18321/ectj1521.

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The Crude Distillation Unit (CDU) mechanism is commonly regarded as the first stage in petroleum refining. In this study, Aspen Plus® is used to simulate the basic process of a CDU, which consists of an Atmospheric Distillation Column (ATC) and a Vacuum Distillation Column (VC). These columns are fed with two types of crude oil: KUMKOL from Kazakhstan and Soviet Export Blend, in the proportions of 0.75:0.25, 0.50:0.50, and 0.25:0.75, respectively. The goal was to do a parametric analysis and analyze the resultant streams of naphtha, kerosene, Atmospheric Gas Oil (AGO), Light Vacuum Gas Oil (LV
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Dissertations / Theses on the topic "Atmospheric Distillation column"

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Yamanishi, Erika. "Simulação, analise e otimização das colunas atmosferica e debutanizadora da unidade de destilação do refino de petroleo." [s.n.], 2007. http://repositorio.unicamp.br/jspui/handle/REPOSIP/267183.

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Orientador: Maria Regina Wolf Maciel<br>Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Quimica<br>Made available in DSpace on 2018-08-08T11:22:24Z (GMT). No. of bitstreams: 1 Yamanishi_Erika_M.pdf: 1072580 bytes, checksum: 5488852fe586d9a1222e4fbf821a946e (MD5) Previous issue date: 2007<br>Resumo: A Unidade de Destilação é uma das mais importantes no refino de petróleo. Sua importância está no fato desta unidade ser responsável pelo fracionamento inicial do petróleo em diversos produtos (frações) como Nafta, Querosene, Diesel, entre outros. Algumas das fr
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Peng, Chi-Chun, and 彭棋俊. "Windows Programming of Binary Distillation Column under Atmospheric Pressure." Thesis, 2012. http://ndltd.ncl.edu.tw/handle/mfb8d7.

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碩士<br>國立臺北科技大學<br>化學工程研究所<br>100<br>The distillation column is a common and important operation unit in the chemical industry. The process utilizes the difference of the boiling point to separate the components. The aim of this research is to develop a program can simulate the steady state of distillation column for different number of stage, feed tray location, flow rate of feed, reflux rate, heat duty. In addition, the dynamic control simulation is also provided. Microsoft Visual Basic 2010 was used to develop the program. The subprograms for solving the mass balance, energy balance and p
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Li, Kuan-Min, and 李冠旻. "Windows Programming of Binary Batch Distillation Column under Atmospheric Pressure." Thesis, 2013. http://ndltd.ncl.edu.tw/handle/gqc932.

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碩士<br>國立臺北科技大學<br>化學工程研究所<br>101<br>Batch Distillation is an important process in chemical industry. Batch distillation is often used to produce small amounts of products with high added value. Most of textbooks focus on the steady state. However, the dynamics operation is more important. 　　The research developed a windows program for binary batch distillation column under atmospheric pressure by Visual Basic 2010. The subprograms for solving the mass balance, energy balance and phase equilibrium equations were constructed firstly. Three strategies for operating the distillate flow rate were a
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Books on the topic "Atmospheric Distillation column"

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Gutzeit, Joerg. Crude Unit Corrosion Guide. 3rd ed. NACE International, The Worldwide Corrosion Authority15835 Park Ten Place Houston, TX 77084, 2016. https://doi.org/10.5006/37612.

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This Guide was written for Plant Operators, Process Engineers, Metallurgists, Maintenance Engineers, Inspectors, and all others who deal with crude unit corrosion and fouling issues on a daily basis. The book is based on the author’s experience dealing with many crude units and also reflects the industry’s consensus experiences reported at past meetings of the former NACE STG34 Committee on Petroleum Refining and Gas Processing and the API Subcommittee on Corrosion and Materials. Diluent recovery units (DRUs) and vacuum distillation units (VDUs) of bitumen upgraders are now included in the dis
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Book chapters on the topic "Atmospheric Distillation column"

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Falkowski, Michał, and Paweł D. Domański. "Nested NARIMA Model of the Atmospheric Distillation Column." In Advances in Intelligent Systems and Computing. Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-13273-6_12.

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Conference papers on the topic "Atmospheric Distillation column"

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Shank, Roxanne A., Thomas R. McCartney, Samar Gharaibeh, and Marcos Panunzio. "Decontamination of a Vacuum Distillation Unit: Mechanical versus Chemical Cleaning; a Case Study." In CORROSION 2017. NACE International, 2017. https://doi.org/10.5006/c2017-09701.

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Abstract Vacuum Distillation is a key aspect of the petroleum refining process, with over 80% of US refineries and nearly all Canadian refineries and upgraders capitalizing on the operational benefits of this unit. A secondary processing unit, the vacuum distillation unit (VDU) receives the heavy bottoms from the atmospheric distillation unit (ADU) and further separates them with the benefit of vacuum pressure to prevent the cracking, or break down, of the oil. The VDU is composed of an outer shell, distillation columns and a fired heat exchanger. When fouled with heavy residuum, the efficienc
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Schutt, H. U., and R. J. Horvath. "Crude Column Overhead Corrosion Problems Caused by Oxidized Sulfur Species." In CORROSION 1987. NACE International, 1987. https://doi.org/10.5006/c1987-87198.

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Abstract Accelerated corrosion experienced in the overhead system of an atmospheric crude distillation column has been analyzed to determine the cause of the corrosion occurring at temperatures above the aqueous dew point. Results of field monitoring tests, laboratory tests and thermodynamic considerations all confirm that the corrosion is caused by deposition of hydrated ammonium bisulfate salts and/or condensation of sulfuric acid. This corrosion can be controlled by reducing the concentration of sulfur oxides in the system, by avoiding operating conditions conducive to formation of these co
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Fan, Deyuan, William C. Fort, and Richard J. Horvath. "Experience with Titanium Heat Exchangers in Refinery Services." In CORROSION 2000. NACE International, 2000. https://doi.org/10.5006/c2000-00691.

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Abstract Several experiences (successful and unsuccessful) with the use of titanium heat exchangers in refining processes are summarized. These experiences primarily involve distillation column overhead condensers in atmospheric crude distilling units, fluid catalytic cracking units, delayed coking units, and sour water strippers. The causes of problems are discussed in relation to known limits of titanium corrosion resistance. Needs for additional data are highlighted.
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Hamza, Ameer, and Rakan M. Samman. "Multiple Tube Failure of Crude Distillation Unit Offgas Inter Stage Coolers." In CONFERENCE 2025. AMPP, 2025. https://doi.org/10.5006/c2025-00549.

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Abstract Crude Distillation Unit (CDU) consist of off-gas compressor which is a two-stage centrifugal machine type with inter and after cooling exchanger. Off-gas from the Pre-flash Column, Atmospheric Column and Vacuum System Liquid ring compressor is combined in the CDU off-gas compressor suction drum. Any condensate or liquid carried over is separated from the gas and pumped with the off-gas compressor suction drum pumps to the discharge line from the second stage. During the analysis of cooling water refinery wide the CDU off-gas compressor inter stage coolers were identified as prime sour
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Soundararajan, Sudharsanan. "Troubleshooting of Main Fractionator Overhead Corrosion in Condensate Splitting Unit Using Ionic Equilibria Modelling." In CONFERENCE 2023. AMPP, 2023. https://doi.org/10.5006/c2023-19325.

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Abstract In a Refinery Condensate Splitting Unit, the lighter Feed hydrocarbon is distillated into Liquified Petroleum Gas, Naphtha, Kerosene, Light &amp; Heavy Gas Oil and Atmospheric Residue. Operating philosophy of this unit is similar to that of Crude Distillation unit but without a desalter. The Pre-flash Column has two stage overhead system, and the Main Fractionator column has Single stage overhead system. Perennial corrosion was experienced in the Main fractionator Overhead fin fan cooler tubes in the form of thinning/pitting due to HCl &amp; Amine/Ammonium chloride salt corrosion. Ion
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Carrillo, José, Juan Pablo Avello, Francisca Sáez, and José R. Pérez-Correa. "Impact of inferential control on the operation of industrial atmospheric distillation columns." In 2024 IEEE International Conference on Automation/XXVI Congress of the Chilean Association of Automatic Control (ICA-ACCA). IEEE, 2024. http://dx.doi.org/10.1109/ica-acca62622.2024.10766755.

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Frantsen, J. E., T. Mathiesen, J. Rau, J. Terävä, P. Björnstedt, and B. Henkel. "Effects of Gas Atmosphere and Surface Quality on Rouging of Three Stainless Steels in WFI." In CORROSION 2003. NACE International, 2003. https://doi.org/10.5006/c2003-03074.

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Abstract The pharmaceutical industry has for a long time been troubled by red-brown to dark violet deposits in distillation columns, storage vessels and distribution systems for water for injection (WFI), hot purified water, and clean steam. This phenomenon is known as rouging due to the visual appearance of the deposits that basically are stainless steel corrosion products. The affected installations are mostly fabricated from the austenitic stainless steel grade AISI 316L. The exact mechanism for rouge formation is not fully understood. However, it is widely reported that the phenomenon is c
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Falkowski, Michal, and Pawel D. Domanski. "Residual analysis of nested NARIMA models of the atmospheric distillation column." In 2019 18th European Control Conference (ECC). IEEE, 2019. http://dx.doi.org/10.23919/ecc.2019.8795950.

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Shulaeva, Ekaterina A., and Lyubov A. Satchikhina. "Optimization of a cascade control loop for circulating irrigation of a distillation column of the atmospheric block of an electric desalting plant." In PROCEEDINGS OF THE III INTERNATIONAL CONFERENCE ON ADVANCED TECHNOLOGIES IN MATERIALS SCIENCE, MECHANICAL AND AUTOMATION ENGINEERING: MIP: Engineering-III – 2021. AIP Publishing, 2021. http://dx.doi.org/10.1063/5.0071753.

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Rivera, W., and J. Cerezo. "Single Stage Heat Transformer Used to Recover Energy in an Oil Distillation Column." In ASME 2001 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2001. http://dx.doi.org/10.1115/imece2001/aes-23623.

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Abstract This paper presents the theoretical analysis of the use of a single stage absorption heat transformer operating with the water-lithium bromide mixture coupled to an oil distillation column installed in a Mexican refinery. The distillation column is used to produce mainly C5H12-1 and C5H12.2. Actually, the heat load in the condenser column is delivered to the atmosphere at 82°C while heat is supplied to the reboiler of the column at 115°C to distill the oil products. In order to reduce the heat load supplied to the reboiler a single stage heat transformer may be coupled of the way that
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