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Relevant bibliographies by topics / Petroleum atmospheric and vacuum distillation

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Academic literature on the topic 'Petroleum atmospheric and vacuum distillation'

Author: Grafiati

Published: 4 June 2021

Last updated: 16 February 2022

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Journal articles on the topic "Petroleum atmospheric and vacuum distillation"

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Yang, Li Min, Hong Hui Zhang, Jia Hao Wang, and Min Hu. "Study on Preparing Light Colored C₉ Petroleum Resins with High Softening Point." Advanced Materials Research 335-336 (September 2011): 899–903. http://dx.doi.org/10.4028/www.scientific.net/amr.335-336.899.

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Polymerizable C9 fraction was cut by atmospheric distillation of raw C9 fraction from thermal cracking. The obtained fraction polymerized using boron trifluoride ethyl ether as catalyst and then the polymerized mixture was washed by warm 10%wt Na2CO3 aqueous solution and distilled water and separated by vacuum distillation for producing light colored C9 petroleum resins with high softening point. The suitable conditions for polymerization process, washing process, vacuum distillation process were investigated to improve the C9 petroleum resins production. Under these conditions, the petroleum

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Nel'kenbaum, S. Ya, R. Z. Safieva, and Ch Kh Sagitova. "Effect of surfactants on atmospheric-vacuum distillation of petroleum systems." Chemistry and Technology of Fuels and Oils 24, no. 6 (1988): 250–52. http://dx.doi.org/10.1007/bf00725593.

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Alrubaye, Saleem Mohammad, Mohammed Saadi Hameed, and Abdulkareem Dahash Affat. "Studying Thermal Cracking Behavior of Vacuum Residue." Iraqi Journal of Chemical and Petroleum Engineering 21, no. 3 (2020): 45–49. http://dx.doi.org/10.31699/ijcpe.2020.3.6.

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In the oil industry, the processing of vacuum residue has an important economic and environmental benefit. This work aims to produce industrial petroleum coke with light fuel fractions (gasoline, kerosene , gas oil) as the main product and de asphalted oil (DAO) as a side production from treatment secondary product matter of vacuum residue. Vacuum residue was produced from the bottom of vacuum distillation unit of the crude oil. Experimentally, the study investigated the effect of the thermal conversion process on (vacuum residue) as a raw material at temperature reaches to 500 °C, pressure 20

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Kim, Myung‐Soo, Jong‐Sic Hwang, and Hyung‐Rak Kim. "Re‐refining of waste lube oils by vacuum distillation with petroleum atmospheric residuum." Journal of Environmental Science and Health . Part A: Environmental Science and Engineering and Toxicology 32, no. 4 (1997): 1013–24. http://dx.doi.org/10.1080/10934529709376593.

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Alrubaye, Saleem Mohammad. "Study the Effect of Catalyst -to- Oil Ratio Parameter (COR) on Catalytic Cracking of Heavy Vacuum Gas Oil." Journal of Engineering 26, no. 7 (2020): 16–27. http://dx.doi.org/10.31026/j.eng.2020.07.02.

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This work deals with the production of light fuel cuts of (gasoline, kerosene and gas oil) by catalytic cracking treatment of secondary product mater (heavy vacuum gas oil) which was produced from the vacuum distillation unit in any petroleum refinery. The objective of this research was to study the effect of the catalyst -to- oil ratio parameter on catalytic cracking process of heavy vacuum gas oil feed at constant temperature (450 °C). The first step of this treatment was, catalytic cracking of this material by constructed batch reactor occupied with auxiliary control devices, at selective r

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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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Imran, Dr Aed Jaber, and Dr Adnan Abdul jabbar. "Increasing production of gasoline and diesel fuel in medium and small refineries to meet the needs of Iraqi market." Journal of Petroleum Research and Studies 7, no. 2 (2021): 46–57. http://dx.doi.org/10.52716/jprs.v7i2.187.

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Iraq is considered one of the countries exporters of oil in the world, but the output of motors fuels from the refined crude oil less than (45 wt %), which is associated with the lack of Iraqi refineries with secondary processes.Iraq consist of five big capacity crude oil refineries which include (atmospheric crude distillation, hydrotreating, catalytic reforming and isomerization) and produce high quality motors fuel, in addition five medium and five small in capacity crude oil refineries include only atmospheric crude distillation which produce low quality raw products (light and heavy napht

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Pleyer, Olga, Dan Vrtiška, Petr Straka, Aleš Vráblík, Jan Jenčík, and Pavel Šimáček. "Hydrocracking of a Heavy Vacuum Gas Oil with Fischer–Tropsch Wax." Energies 13, no. 20 (2020): 5497. http://dx.doi.org/10.3390/en13205497.

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Catalytic hydrocracking represents an optimal process for both heavy petroleum fractions and Fischer–Tropsch (FT) wax upgrading because it offers high flexibility regarding the feedstock, reaction conditions and products’ quality. The hydrocracking of a heavy vacuum gas oil with FT wax was carried out in a continuous-flow catalytic unit with a fixed-bed reactor and a co-current flow of the feedstock and hydrogen at the reaction temperatures of 390, 400 and 410 °C and a pressure of 8 MPa. The increasing reaction temperature and content of the FT wax in the feedstock caused an increasing yield i

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Azis, Zarkoni, Bambang Heru Susanto, and Mohammad Nasikin. "Gasoline Yield Enhancement in Fluid Catalytic Cracking by Coprocessing of Petroleum Gasoil with Refined Bleached Deodorized Palm Oil and Palm Fatty Acid Distillate." Journal of Computational and Theoretical Nanoscience 17, no. 2 (2020): 1079–84. http://dx.doi.org/10.1166/jctn.2020.8770.

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Gasoline is liquid hydrocarbon fuel used for spark-ignition engine. Most of gasoline production is carried out in the petroleum oil refinery through several stages of process and fluid catalytic cracking (FCC) is an important process that can convert some of heavy oil fractions like vacuum gasoil (VGO) and residue to be cracked into gasoline and lighter products. Consumption of gasoline for transportation fuel in Indonesia is higher than its production capability, so this gap has compelled to search the alternative process route using renewable feedstock. Coprocessing of petroleum gasoil with

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Saifullin, N. R., and R. G. Gareev. "High-vacuum “dry” distillation of atmospheric resid." Chemistry and Technology of Fuels and Oils 35, no. 6 (1999): 333–37. http://dx.doi.org/10.1007/bf02694091.

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Dissertations / Theses on the topic "Petroleum atmospheric and vacuum distillation"

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El, Gemayel Gemayel. "Integration and Simulation of a Bitumen Upgrading Facility and an IGCC Process with Carbon Capture." Thèse, Université d'Ottawa / University of Ottawa, 2012. http://hdl.handle.net/10393/23274.

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Hydrocracking and hydrotreating are bitumen upgrading technologies designed to enhance fuel quality by decreasing its density, viscosity, boiling point and heteroatom content via hydrogen addition. The aim of this thesis is to model and simulate an upgrading and integrated gasification combined cycle then to evaluate the feasibility of integrating slurry hydrocracking, trickle-bed hydrotreating and residue gasification using the Aspen HYSYS® simulation software. The close-coupling of the bitumen upgrading facilities with gasification should lead to a hydrogen, steam and power self-sufficient u

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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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Sotelo, Francisco Falla. "Aplicação da espectroscopia de infravermelho próximo na caracterização de petróleo: simulação de uma unidade de destilação atmosférica." Universidade de São Paulo, 2006. http://www.teses.usp.br/teses/disponiveis/3/3137/tde-13032007-002338/.

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A contínua mudança na qualidade da carga de alimentação das unidades de destilação atmosférica introduz incertezas na operação do processo de refino. A caracterização precisa do petróleo bruto, cuja composição varia devido à sua natureza intrínseca e às condições de transporte e armazenamento nas refinarias, poderia auxiliar na redução destas incertezas. O processo clássico de caracterização, baseado nas curvas de destilação TBP (True Boiling Point, Ponto de Ebulição Verdadeiro), ainda não permite detectar essas mudanças de modo mais dinâmico, o que reduz a precisão da simulação do processo e,

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Book chapters on the topic "Petroleum atmospheric and vacuum distillation"

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Jones, David S. "Atmospheric and Vacuum Crude Distillation Units in Petroleum Refineries." In Handbook of Petroleum Processing. Springer International Publishing, 2014. http://dx.doi.org/10.1007/978-3-319-05545-9_25-1.

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Jones, David S. J. "Atmospheric and Vacuum Crude Distillation Units in Petroleum Refineries." In Handbook of Petroleum Processing. Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-14529-7_25.

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Cai, Baoping, Yonghong Liu, Zengkai Liu, Yuanjiang Chang, and Lei Jiang. "Bayesian Network-Based Risk Analysis Methodology: A Case of Atmospheric and Vacuum Distillation Unit." In Bayesian Networks for Reliability Engineering. Springer Singapore, 2019. http://dx.doi.org/10.1007/978-981-13-6516-4_9.

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Osuolale, Funmilayo N., and Jie Zhang. "Exergetic Optimisation of Atmospheric and Vacuum Distillation System Based on Bootstrap Aggregated Neural Network Models." In Exergy for A Better Environment and Improved Sustainability 1. Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-62572-0_66.

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Alshehri, Feras Ahmed, Saeed M. Al-Shihri, Mohammed C. Al-Kinany, et al. "Advanced Catalysis and Processes to Convert Heavy Residues Into Fuels and High Value Chemicals." In Advanced Catalysis Processes in Petrochemicals and Petroleum Refining. IGI Global, 2020. http://dx.doi.org/10.4018/978-1-5225-8033-1.ch004.

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The petroleum refining process begins with distillation, first at atmospheric pressure and after at reduced pressure. The volatile fractions, in both cases, have greater economic value, and the distillation residue-produced atmospheric residue and vacuum residue represent a significant portion of a barrel of crude. The need to convert bottom of the barrel into cleaner and more valuable olefins and liquid products is continuously increasing. Thus, residue must be converted into more valuable products, and further processes can be employed for upgrading residue. Examples are delayed coking, visco-reduction, and fluidized catalytic cracking. On the other hand, the optimization of refining facilities to deal with such feeds brings economic competitiveness since these oils have low prices in the international market. Studies on processes and catalytic cracking are quite important under this aspect. The conversion of heavy petroleum fraction into valuable liquid products and high value chemicals has been important objectives for upgrading heavy petroleum oils.

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"Vacuum Distillation Unit." In Petroleum Refinery Process Modeling - Integrated Optimization Tools and Applications. Wiley-VCH Verlag GmbH & Co. KGaA, 2018. http://dx.doi.org/10.1002/9783527813391.ch3.

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"Atmospheric or Crude Distillation Unit (CDU)." In Petroleum Refinery Process Modeling - Integrated Optimization Tools and Applications. Wiley-VCH Verlag GmbH & Co. KGaA, 2018. http://dx.doi.org/10.1002/9783527813391.ch2.

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Conference papers on the topic "Petroleum atmospheric and vacuum distillation"

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Zhang, Shuzhan, Dongya Zhao, Sarah K. Spurgeon, and Xinggang Yan. "Distributed model predictive control for the atmospheric and vacuum distillation towers in a petroleum refining process." In 2016 UKACC 11th International Conference on Control (CONTROL). IEEE, 2016. http://dx.doi.org/10.1109/control.2016.7737534.

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Osuki, Takahiro, Masahiro Seto, Hirokazu Okada, Masayuki Sagara, Satoshi Matsumoto, and Toshihide Ono. "Development of Fit-for-Purpose Austenitic Stainless Steels With High Polythionic Acid Stress Corrosion Resistance." In ASME 2017 Pressure Vessels and Piping Conference. American Society of Mechanical Engineers, 2017. http://dx.doi.org/10.1115/pvp2017-65536.

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In the process units with Polythionic Acid Stress Corrosion Cracking (PTA-SCC) such as hydrotreater or hydrocracker, the neutralization treatment like soda ash washing and/or PWHT, Post Weld Heat Treatment, are conducted for stabilized austenitic stainless steels of TP321H or TP347H to mitigate the potential of PTA-SCC. 347AP, the proprietary version of Type 347LN, is remarkable for the possibility to save the fabrication and turnaround cost by the elimination of the neutralization treatment and/or PWHT and its reliability to PTA-SCC resistance without PWHT and neutralization was proven by the

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Zhang, Junyan, Baoping Cai, Yiliu Liu, and Min Xie. "Risk analysis of atmospheric and vacuum distillation unit using Bayesian networks." In 2016 11th International Conference on Reliability, Maintainability and Safety (ICRMS). IEEE, 2016. http://dx.doi.org/10.1109/icrms.2016.8050046.

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de Oliveira, Peterson Machado, Cristiano Vitorino da Silva, and Flavia Zinani. "CFD analysis of the temperature profile in a petroleum atmospheric distillation furnace chamber." In XXXVIII Iberian-Latin American Congress on Computational Methods in Engineering. ABMEC Brazilian Association of Computational Methods in Engineering, 2017. http://dx.doi.org/10.20906/cps/cilamce2017-0774.

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Kandasamy, V., I. Idris, A. Abdullah, I. K. Shamsudin, L. C. Law, and M. R. Othman. "Optimizing atmospheric distillation unit for maximum light petroleum gas yield and comparative case studies." In 6TH INTERNATIONAL CONFERENCE ON ENVIRONMENT (ICENV2018): Empowering Environment and Sustainable Engineering Nexus Through Green Technology. AIP Publishing, 2019. http://dx.doi.org/10.1063/1.5117110.

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Li, Xiang, Cheng Dai, Feng Gao, Huadong Wang, and Zhimin Sun. "Application of Failure Mode and Effect Analysis on Centrifugal Pumps of Atmospheric and Vacuum Distillation Unit." In ASME 2018 Pressure Vessels and Piping Conference. American Society of Mechanical Engineers, 2018. http://dx.doi.org/10.1115/pvp2018-85008.

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A failure mode and effect analysis is performed on 58 centrifugal pumps of Atmospheric and Vacuum Distillation Unit in one of the plants of SINOPEC. Firstly, the failure modes of the pumps are classified. Then, the failure causes of the pumps are analyzed. After that, the influence of the failure and the risk level are determined. Finally, the maintenance strategies to reduce risk are put forward according to the equipment failure mode and risk level, which is the basis for the maintenance of pumps. The results show that the main failure modes of the centrifugal pumps are process medium leakag

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Kopytov, Mikhail A., and Anatoly K. Golovko. "Structural group characteristics of resins and asphaltenes of heavy oils and their atmospheric-vacuum distillation residues." In PROCEEDINGS OF THE INTERNATIONAL CONFERENCE ON ADVANCED MATERIALS WITH HIERARCHICAL STRUCTURE FOR NEW TECHNOLOGIES AND RELIABLE STRUCTURES 2019. AIP Publishing, 2019. http://dx.doi.org/10.1063/1.5132036.

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Zhao, Liang, Zexin Zhang, Lida Wang, and Guichang Liu. "Design of High Temperature Anticorrosion Diagnosis System for Atmospheric and Vacuum Distillation Unit Based on Forcecontrol and SQL Sever2014." In 2020 5th International Conference on Automation, Control and Robotics Engineering (CACRE). IEEE, 2020. http://dx.doi.org/10.1109/cacre50138.2020.9230239.

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Zilberman, Boris Ya, Mikhail N. Makarychev-Mikhailov, Vladimir F. Saprykin, Stanislav V. Sakulin, Yury N. Dulepov, and Vladimir V. Glushko. "Methods of Radical Regeneration of Spent Solvent Containing TBP and Diluent." In ASME 2001 8th International Conference on Radioactive Waste Management and Environmental Remediation. American Society of Mechanical Engineers, 2001. http://dx.doi.org/10.1115/icem2001-1303.

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Abstract Methods of steam-supported distillation of spent solvent containing 30% tributyl phosphate (TBP) in various diluents have been developed. Single-stage and two-stage processes were tested. Single-stage distillation can be realized either with the use of superheated steam under vacuum or with saturated steam at atmospheric pressure, ensuring transportation of all the solvent to distillate, independently of the used diluent. Two-stage process allows separating TBP and diluent, both of them being purified, when the diluent boiling temperature is 50–70°C below TBP boiling point. At the fir

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Ritchey, Susan N. "Shellside Vacuum Condensation With a Noncondensable Gas." In ASME 2016 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2016. http://dx.doi.org/10.1115/imece2016-67417.

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Shell-and-tube vacuum condensers are present in many industrial applications such as chemical manufacturing, distillation, and power production [1–3]. They are often used because operating a condenser under vacuum pressures can increase the efficiency of energy conversion, which increases the overall plant efficiency and saves money. Typical operating pressures in the petrochemical industry span a wide range of values, from one atmosphere (101.3 kPa) down to a medium vacuum (1 kPa). The current shellside condensation methods used to predict heat transfer coefficients are based on data collecte

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