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Journal articles on the topic 'Petroleum chemistry/refining'

Author: Grafiati

Published: 4 June 2021

Last updated: 1 February 2022

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1

Kapustin, V. M., and E. A. Chernysheva. "The development of petroleum refining and petroleum chemistry in Russia." Petroleum Chemistry 50, no. 4 (July 2010): 247–54. http://dx.doi.org/10.1134/s0965544110040018.

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2

Klokova, T. P., O. F. Glagoleva, N. K. Matveeva, and Yu A. Volodin. "Surfactants in petroleum refining processes." Chemistry and Technology of Fuels and Oils 33, no. 1 (January 1997): 6–8. http://dx.doi.org/10.1007/bf02768130.

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3

Öhlmann, G. "Catalysts in Petroleum Refining and Petrochemical Industries 1995." Zeitschrift für Physikalische Chemie 203, Part_1_2 (January 1998): 252–54. http://dx.doi.org/10.1524/zpch.1998.203.part_1_2.252.

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4

Levinbuk, M. I., E. F. Kaminskii, and O. F. Glagoleva. "Some problems of petroleum refining in Russia." Chemistry and Technology of Fuels and Oils 36, no. 2 (March 2000): 69–77. http://dx.doi.org/10.1007/bf02725252.

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5

Nefedov, B. K. "High-silica zeolites in petroleum refining processes." Chemistry and Technology of Fuels and Oils 21, no. 9 (September 1985): 457–61. http://dx.doi.org/10.1007/bf00735120.

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6

Popovic, Zoran, Ivan Soucek, Nickolay Ostrovskii, and Ozren Ocic. "Whether integrating refining and petrochemical business can provide opportunities for development of petrochemical industry in Serbia." Chemical Industry 70, no. 3 (2016): 307–18. http://dx.doi.org/10.2298/hemind150122037p.

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Since the beginning of 90s of last century both the petroleum industry and petrochemical industry have operated in difficult circumstances. In particularly, margins of petroleum and petrochemical industry were exacerbated during global economic crisis in 2008-2009 years. At that time, as one option that could be the solution, the global analysts had started to more intense investigate the benefits of Refining-Petrochemical Integration. Shortly afterwards, more and more petroleum refineries and petrochemical manufacturers began to see the future in this kind of operational, managerial, marketing and commercial connection. This paper evaluates, in particular, the achieved level of integration of refinery and petrochemical businesses in Central and South-Eastern Europe. And specifically, the paper identifies current capabilities and future chances of linking this kind of integration between Serbian refining and petrochemical players. The viability of integration between possible actors and benefits of every single refining-petrochemical interface in Serbia depend on many factors, and therefore each integrated system is unique and requires prior serious Cost Benefit Analysis.

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7

Shah, Nikisha K., Zukui Li, and Marianthi G. Ierapetritou. "Petroleum Refining Operations: Key Issues, Advances, and Opportunities." Industrial & Engineering Chemistry Research 50, no. 3 (February 2, 2011): 1161–70. http://dx.doi.org/10.1021/ie1010004.

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8

Wu, C., Y. Cheng, and Y. Jin. "Downer-to-Riser Coupling Technique for Petroleum Refining." Chemical Engineering & Technology 32, no. 3 (March 2009): 482–91. http://dx.doi.org/10.1002/ceat.200800563.

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9

Kondrasheva, N. K. "Marine fuels from products of deep petroleum refining." Chemistry and Technology of Fuels and Oils 25, no. 11 (November 1989): 529–35. http://dx.doi.org/10.1007/bf00726818.

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10

Goberis, S. Yu, and A. B. Shtuopis. "Heat-resistant concretes containing spent catalyst of petroleum refining." Refractories and Industrial Ceramics 38, no. 1 (January 1997): 23–26. http://dx.doi.org/10.1007/bf02768230.

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11

Shah, Raj, Richard Ashby, and Nathan Aragon. "Advancements and further research trends for microbial biosurfactants in the petroleum industry." INFORM International News on Fats, Oils, and Related Materials 32, no. 5 (May 1, 2021): 12–16. http://dx.doi.org/10.21748/inform.05.2021.12.

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Surfactants are widely used in the petroleum industry during many stages of oil recovery, refining and spill cleanup. Because these processes release surfactants directly into the environment, much research has been done on the potential for replacing the more commonly used synthetic surfactants with more eco-friendly biosurfactants.This article highlights some recent studies of the effectiveness of biosurfactants applied to various aspects of the petroleum industry.

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12

Han, Jeongwoo, Grant S. Forman, Amgad Elgowainy, Hao Cai, Michael Wang, and Vincent B. DiVita. "A comparative assessment of resource efficiency in petroleum refining." Fuel 157 (October 2015): 292–98. http://dx.doi.org/10.1016/j.fuel.2015.03.038.

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13

Kaminskii, �. F., I. T. Kozlov, and S. G. Ashitko. "The Petroleum Refining Industry of Russia: Today and tomorrow." Chemistry and Technology of Fuels and Oils 29, no. 9 (September 1993): 413–16. http://dx.doi.org/10.1007/bf00723191.

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14

Park, Dong Ho, Seong Su Kim, Hui Wang, Thomas J Pinnavaia, Maria C Papapetrou, Angelos A Lappas, and Kostas S Triantafyllidis. "Selective Petroleum Refining Over a Zeolite Catalyst with Small Intracrystal Mesopores." Angewandte Chemie International Edition 48, no. 41 (September 28, 2009): 7645–48. http://dx.doi.org/10.1002/anie.200901551.

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15

Ptak, Stefan, Wojciech Krasodomski, Janusz Jakóbiec, and Artur Antosz. "Modified TDAE petroleum plasticiser." Open Chemistry 19, no. 1 (January 1, 2021): 916–28. http://dx.doi.org/10.1515/chem-2021-0081.

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Abstract Petroleum plasticisers are applied as softening additives in rubber vulcanisation processes and as components of rubber mixtures in the production and vulcanisation process. They contain polycyclic aromatic compounds exhibiting carcinogenic and mutagenic effects. Since 2010, the European Union has banned the use of high-aromatic DAE plasticisers. The petroleum industry and tyre manufacturers are developing new types of petroleum plasticisers. The best alternative to the DAE is the TDAE plasticisers, obtained mainly by selective solvent refining. The solvent dewaxing process of classic TDAE plasticisers was studied in order to improve the chemical composition as well as the rheological and low-temperature properties of deparafinate. This article presents the results of an examination of the TDAE plasticiser samples subjected to solvent dewaxing process on a laboratory scale with three types of solvents, MEK–TOL, MEK–MIBK and MEK–MTBE. It was demonstrated that solvent dewaxing of the TDAE plasticiser with positive pour points maintains good process selectivity and allows for a significant reduction of the plasticiser pour point, thus improving the rheological and low-temperature properties. In all dewaxing attempts, the pour point in the deparaffinate decreased significantly to the range −12 to −22°C, compared to the positive pour points of the raw materials. The application tests for two types of the TDAE plasticisers, used to produce oiled rubber and a standard rubber compound, meet the quality requirements for those products.

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16

Dolmatov, L. V. "Petroleum pitch recovery as a means of intensifying oil refining." Chemistry and Technology of Fuels and Oils 25, no. 7 (July 1989): 338–39. http://dx.doi.org/10.1007/bf00719332.

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17

Prokhorova, A. A. "Petroleum refining industry of developed capitalist countries in the 1990s." Chemistry and Technology of Fuels and Oils 29, no. 11 (November 1993): 561–71. http://dx.doi.org/10.1007/bf00723971.

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18

Joseph, Dr Elizabeth. "Re–Refining of Used Lube Oils and Sustainability." International Journal for Research in Applied Science and Engineering Technology 9, no. VI (June 30, 2021): 4609–13. http://dx.doi.org/10.22214/ijraset.2021.35855.

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As petroleum products continue to be an inseparable part of our lives, so does the waste that is generated from these products, the prominent among them being the used lubricating oil. However, research shows that more than half of the used lube oil can be converted back to usable lubricant through the process of re–refining. This can certainly reduce the amount of waste oil in the environment and the need of crude oil extraction to a certain extent. As there are various different methods of re–refining, this work focused specifically on the method used widely in India, i.e., Vacuum distillation with Clay treatment. In this paper, the sustainability of the re–refining process was checked using the green chemistry principles and overall material balance of the process. Based on the assumptions made for the material balance, nearly 69.92% of lube oil base stock was obtained along with 11.13% fuel by - product and 12.14% residue, both of which have varied uses in the industry, thus producing additional profit.

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19

Hueso, José L., Víctor J. Rico, José Cotrino, J. M. Jiménez-Mateos, and Agustín R. González-Elipe. "Water plasmas for the revalorisation of heavy oils and cokes from petroleum refining." Environmental Science & Technology 43, no. 7 (April 2009): 2557–62. http://dx.doi.org/10.1021/es900236b.

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20

Cataldo, Franco, Yeghis Keheyan, and Dieter Heymann. "A new model for the interpretation of the unidentified infrared bands (UIBS) of the diffuse interstellar medium and of the protoplanetary nebulae." International Journal of Astrobiology 1, no. 2 (April 2002): 79–86. http://dx.doi.org/10.1017/s1473550402001131.

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In this work we started from the basic idea that the pure polycyclic aromatic hydrocarbons (PAHs) cannot be the real carriers of the unidentified infrared bands (UIBs), the emission spectra coming from a large variety of astronomical objects. Instead we propose a new model taken from petroleum chemistry which, we can show, is able to match both the UIBs and even the protoplanetary nebulae (PPNe) spectra. PAHs such as phenanthrene, benzoperylene, coronene and pentacene, are too pure and too specific to really exist in the interstellar medium. Instead our model proposes that the carrier of UIBs and PPNe are complex molecular mixtures like those obtained as fractions during the petroleum refining processes. These molecular mixtures are so complex that practically the investigators did not try to identify each individual component but characterized the mixture with an average molecular structure that takes into account both the average molecular weight and the average content of aromatic, naphtenic (cycloaliphatic) and aliphatic (paraffinic) fraction. We show by infrared spectroscopy that petroleum fractions obtained at certain steps of the refining process are able to match the UIBs and the PPNe infrared bands with the advantage of not being so specific as PAHs are. Namely we have used as samples a distillate aromatic extract (DAE) a treated residual aromatic extract (T-RAE) and finally a naphtenic oil. Among the three samples examined, the DAE sample was the best in matching the UIBs and PPNe spectra.

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21

Wang, Bing, Rui Xiao, and Huiyan Zhang. "An Overview of Bio-oil Upgrading with High Hydrogen-containing Feedstocks to Produce Transportation Fuels: Chemistry, Catalysts, and Engineering." Current Organic Chemistry 23, no. 7 (July 16, 2019): 746–67. http://dx.doi.org/10.2174/1385272823666190405145007.

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As an alternative to increasingly depleted traditional petroleum fuel, bio-oil has many advantages: high energy density, flexibility, easy storage and transportation. Nevertheless, bio-oil also presents some unwanted characteristics such as high viscosity, acidity, oxygen content and chemical instability. The process of bio-oil upgrading is necessary before utilization as transportation fuels. In addition, the bio-oil has low effective hydrogen/ carbon molar ratio (H/Ceff) which may lead to coke formation and hence deactivation of the catalyst during the upgrading process. Therefore, it seemed that co-refining of biooil with other higher hydrogen-containing feedstocks is necessary. This paper provides a broad review of the bio-oil upgrading with high hydrogen-containing feedstocks to produce transportation fuels: chemistry, catalyst, and engineering research aspects were discussed. The different thermochemical conversion routes to produce bio-oil and its physical-chemical properties are discussed firstly. Then the bio-oil upgrading research using traditional technologies and common catalysts that emerged in recent years are briefly reviewed. Furthermore, the applications of high H/Ceff feedstock to produce high-quality of bio-oil are also discussed. Moreover, the emphasis is placed on co-refining technologies to produce transportation fuels. The processes of co-refining bio-oil and vacuum gas oil in fluid catalytic cracking (FCC) unit for transportation fuels from laboratory scale to pilot scale are also covered in this review. Co-refining technology makes it possible for commercial applications of bio-oil. Finally, some suggestions and prospects are put forward.

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22

Abramova, A. V., E. V. Slivinskii, Yu Ya Goldfarb, A. A. Panin, E. A. Kulikova, and G. A. Kliger. "Development of Efficient Zeolite-Containing Catalysts for Petroleum Refining and Petrochemistry." Kinetics and Catalysis 46, no. 5 (September 2005): 758–69. http://dx.doi.org/10.1007/s10975-005-0133-5.

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23

Vasil'eva, I. I., E. T. Klimenko, G. M. Tatarintseva, and O. V. Fonin. "Development of petroleum-refining process control systems based on kinetic models." Chemistry and Technology of Fuels and Oils 26, no. 5 (May 1990): 213–15. http://dx.doi.org/10.1007/bf01163882.

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24

Nefedov, B. K., T. V. Alekseeva, and I. E. Gorbatkina. "Synthetic zeolites and zeolitic catalysis in petroleum refining and petrochemical production." Chemistry and Technology of Fuels and Oils 29, no. 9 (September 1993): 429–36. http://dx.doi.org/10.1007/bf00723195.

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25

Nefedov, B. K. "Problems in deactivation of catalysts for hydrogenation processes in petroleum refining." Chemistry and Technology of Fuels and Oils 27, no. 2 (February 1991): 73–85. http://dx.doi.org/10.1007/bf00725063.

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26

Zubarev, S. V., N. A. Alekseeva, V. N. Ivashentsev, G. P. Yavshits, V. I. Matyushkin, A. I. Bon, and I. I. Shishova. "Purification of waste water in petroleum refining industries by membrane methods." Chemistry and Technology of Fuels and Oils 25, no. 11 (November 1989): 588–92. http://dx.doi.org/10.1007/bf00726834.

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27

Ponomareva, O. A., I. A. Kasyanov, E. E. Knyazeva, S. V. Konnov, and I. I. Ivanova. "Effect of the degree of zeolite recrystallization into micro–mesoporous materials on their catalytic properties in petroleum refining and petroleum chemistry processes." Petroleum Chemistry 56, no. 9 (September 2016): 819–26. http://dx.doi.org/10.1134/s0965544116090188.

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28

Ho, Chii-Dong, Yih-Hang Chen, Chao-Min Chang, and Hsuan Chang. "Evaluation of Process Control Schemes for Sour Water Strippers in Petroleum Refining." Processes 9, no. 2 (February 16, 2021): 363. http://dx.doi.org/10.3390/pr9020363.

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For the sour water strippers in petroleum refinery plants, three prediction models were developed first, including the estimators of sour water feed concentrations using convenient online measurements, the minimum reboiler duty and the corresponding internal temperature at a specific location (Tstage,29). Feedforward control schemes were developed based on these prediction models. Four categories of control schemes, including feedforward, feedback, feedback with external reset, and feedforward-feedback, were proposed and evaluated by the rigorous dynamic simulation model of the sour water stripper for their dynamic responses to the sour water feed stream disturbances. The comparison of control performance, in terms of the settling time, integrated absolute error (IAE) of the NH3 concentration of the stripped sour water and IAE of the specific reboiler duty, reveals that FFT (feedforward control of Tstage,29) and FBA-DT3 (feedback control with 3 min concentration measurement delay) are the best control schemes. The second-best control scheme is FBAT (cascade feedback control of concentration with temperature).

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29

Khaliullin, Alexey K., Kseniya S. Trofimova, and Mikhail G. Voronkov. "Production of Sulfur-Containing Polymers on the Basis of Petroleum Refining and Chloroorganic Wastes." Phosphorus, Sulfur, and Silicon and the Related Elements 153, no. 1 (January 1999): 421–22. http://dx.doi.org/10.1080/10426509908546501.

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30

Asaftei, Iuliean V., Ion Sandu, Nicolae Bilba, Neculai Catalin Lungu, Maria Ignat, and Elvira Mahu. "Oligo-Aromatization of Light Hydrocarbons from Petroleum Refining Processes Over ZnO/MFI Microporous Material." Revista de Chimie 71, no. 2 (March 3, 2020): 403–12. http://dx.doi.org/10.37358/rc.20.2.7943.

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The conversion of light hydrocarbons resulted as by-product of petroleum refining (mixtures of (n + i) butanes, 52.28 � 63.20 vol.%, (1-, cis-, trans-, 2-) butenes, 28.64 � 36.43 vol.% and propane � propylene, 4.79 � 14.64 vol.%) over bifunctional 5% ZnO/HZSM-5 co-catalyst in a fixed-bed stainless-steel reactor (Twin Reactor System Naky) at 450�C, 4 atm. total pressure and at a space velocity (WHSV) of 1 h-1 have been investigated. The results indicate that the selectivity to light aromatics � benzene, toluene and xylenes (BTX) � and to both the gaseous C1, C2 - C4 hydrocarbons and liquid (i + n) C5 � C10 aliphatic hydrocarbons depends on the time on stream of the process. This is a result of coke deposition (polyunsaturated compounds) and catalyst deactivation. The aromatics BTX represent 59-60 wt% in the liquid product during the first 24-36 hours time-on-stream and only 20-30 wt% after 40 hours of reaction when the aliphatic hydrocarbon C5 � C10 (mostly iso) and ]C10 (denoted �oligo�) reach to 70 � 80 wt%. The aromatic products were principally toluene, xylenes and benzene, theirs concentration varying with the time on stream of the process. The initial aromatization process described as dehydrocyclodimerization of alkanes and alkenes, principally to aromatics BTX and molecular hydrogen is accompanied by an oligomerization, isomerisation, cracking and alkylation process to form finally in the liquid product an excessively mixture of iso- and normal- C5 � C10 aliphatic hydrocarbons and ] C10.

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31

Dorogochinskii, A. Z. "The birth and growth of the Grozny petroleum refining and petrochemical industry." Chemistry and Technology of Fuels and Oils 29, no. 12 (December 1993): 602–8. http://dx.doi.org/10.1007/bf00727135.

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32

Elmobarak, Wamda Faisal, Bassim H. Hameed, Fares Almomani, and Ahmad Zuhairi Abdullah. "A Review on the Treatment of Petroleum Refinery Wastewater Using Advanced Oxidation Processes." Catalysts 11, no. 7 (June 27, 2021): 782. http://dx.doi.org/10.3390/catal11070782.

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The petroleum industry is one of the most rapidly developing industries and is projected to grow faster in the coming years. The recent environmental activities and global requirements for cleaner methods are pushing the petroleum refining industries for the use of green techniques and industrial wastewater treatment. Petroleum industry wastewater contains a broad diversity of contaminants such as petroleum hydrocarbons, oil and grease, phenol, ammonia, sulfides, and other organic composites, etc. All of these compounds within discharged water from the petroleum industry exist in an extremely complicated form, which is unsafe for the environment. Conventional treatment systems treating refinery wastewater have shown major drawbacks including low efficiency, high capital and operating cost, and sensitivity to low biodegradability and toxicity. The advanced oxidation process (AOP) method is one of the methods applied for petroleum refinery wastewater treatment. The objective of this work is to review the current application of AOP technologies in the treatment of petroleum industry wastewater. The petroleum wastewater treatment using AOP methods includes Fenton and photo-Fenton, H2O2/UV, photocatalysis, ozonation, and biological processes. This review reports that the treatment efficiencies strongly depend on the chosen AOP type, the physical and chemical properties of target contaminants, and the operating conditions. It is reported that other mechanisms, as well as hydroxyl radical oxidation, might occur throughout the AOP treatment and donate to the decrease in target contaminants. Mainly, the recent advances in the AOP treatment of petroleum wastewater are discussed. Moreover, the review identifies scientific literature on knowledge gaps, and future research ways are provided to assess the effects of these technologies in the treatment of petroleum wastewater.

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33

Lin, Boqiang, and Miao Wang. "Dynamic analysis of carbon dioxide emissions in China's petroleum refining and coking industry." Science of The Total Environment 671 (June 2019): 937–47. http://dx.doi.org/10.1016/j.scitotenv.2019.03.321.

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34

Madeti, Madhavi, Sharad V. Lande, Kalpana G, R. K. Mewada, and R. V. Jasra. "A Green Approach." International Journal of Green Nanotechnology 1 (January 1, 2013): 194308921350702. http://dx.doi.org/10.1177/1943089213507024.

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We have attempted a green alternative to reuse the spent fluid catalytic cracking (FCC) catalyst that is used in petroleum refining industry for the upgradation and purification of various petroleum streams and residues. The spent FCC zeolite–based catalyst modified by enhancing the acidic properties by incorporating Zn and In metals in the matrix. The various prepared catalysts were systematically characterized by X-ray powder diffraction and Brunauer–Emmett–Teller (BET; adsorption isotherm) surface area. The acidity of the materials was studied by temperature-programmed desorption of ammonia (NH3-TPD). The well-characterized catalysts were applied for liquid phase benzylation of o-xylene using benzyl chloride.

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35

Gorbatkina, I. E., B. K. Nefedov, N. N. Rostanin, L. D. Konoval'chikov, and E. D. Rostanina. "Low-alkali zeolite TsVN-an effective catalyst in petroleum refining and petrochemical processes." Chemistry and Technology of Fuels and Oils 28, no. 12 (December 1992): 655–59. http://dx.doi.org/10.1007/bf00729568.

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36

Mikhol’skaya, I. N., E. A. Danilova, N. S. Osinskaya, A. A. Borisova, V. V. Spaskova, and B. S. Zhirnov. "Monitoring the Ecosystem Near Petroleum Refining and Petrochemical Plants in an Urban Environment." Chemistry and Technology of Fuels and Oils 57, no. 3 (July 2021): 477–81. http://dx.doi.org/10.1007/s10553-021-01269-0.

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37

Fu, Haihui, Yan Chen, Tingting Liu, Xuemei Zhu, Yufei Yang, and Haitao Song. "Research on Hazardous Waste Removal Management: Identification of the Hazardous Characteristics of Fluid Catalytic Cracking Spent Catalysts." Molecules 26, no. 8 (April 15, 2021): 2289. http://dx.doi.org/10.3390/molecules26082289.

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Fluid catalytic cracking (FCC) spent catalysts are the most common catalysts produced by the petroleum refining industry in China. The National Hazardous Waste List (2016 edition) lists FCC spent catalysts as hazardous waste, but this listing is very controversial in the petroleum refining industry. This study collects samples of waste catalysts from seven domestic catalytic cracking units without antimony-based passivation agents and identifies their hazardous characteristics. FCC spent catalysts do not have the characteristics of flammability, corrosiveness, reactivity, or infectivity. Based on our analysis of the components and production process of the FCC spent catalysts, we focused on the hazardous characteristic of toxicity. Our results show that the leaching toxicity of the heavy metal pollutants nickel, copper, lead, and zinc in the FCC spent catalyst samples did not exceed the hazardous waste identification standards. Assuming that the standards for antimony and vanadium leachate are 100 times higher than that of the surface water and groundwater environmental quality standards, the leaching concentration of antimony and vanadium in the FCC spent catalyst of the G set of installations exceeds the standard, which may affect the environmental quality of surface water or groundwater. The quantities of toxic substances in all spent FCC catalysts, except those from G2, does not exceed the standard. The acute toxicity of FCC spent catalysts in all installations does not exceed the standard. Therefore, we exclude “waste catalysts from catalytic cracking units without antimony-based passivating agent passivation nickel agent” from the “National Hazardous Waste List.”

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38

Naranov, E. R., K. I. Dement’ev, I. M. Gerzeliev, N. V. Kolesnichenko, E. A. Roldugina, and A. L. Maksimov. "The Role of Zeolite Catalysis in Modern Petroleum Refining: Contribution from Domestic Technologies." Petroleum Chemistry 59, no. 3 (March 2019): 247–61. http://dx.doi.org/10.1134/s0965544119030101.

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39

Taketomi, S., A. T. Yokobori, K. Takei, Y. Wada, Y. Tanaka, and T. Iwadate. "Corrosion Fatigue Crack Growth Rate for Petroleum Refining Pressure Vessel Materials (2.25Cr-1Mo Steel)." CORROSION 64, no. 9 (September 2008): 744–50. http://dx.doi.org/10.5006/1.3278512.

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40

Elkamel, A., M. Ba-Shammakh, P. Douglas, and E. Croiset. "An Optimization Approach for Integrating Planning and CO2Emission Reduction in the Petroleum Refining Industry." Industrial & Engineering Chemistry Research 47, no. 3 (February 2008): 760–76. http://dx.doi.org/10.1021/ie070426n.

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41

Wang, Di, Jia Guo, Ming Su, Jun Sun, Sheng Zhang, Wantai Yang, Xiaoyu Gu, and Hongfei Li. "The Application of a Novel Char Source From Petroleum Refining Waste in Flame Retardant Thermoplastic Polyurethane." Polymer Engineering & Science 60, no. 5 (February 25, 2020): 1029–34. http://dx.doi.org/10.1002/pen.25358.

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42

Firouzjaee, Mahjoobeh Hajitabar, and Majid Taghizadeh. "Synthesis Procedure and Industrial Applications of NaY Zeolite for Various Processes: A Review." Mini-Reviews in Organic Chemistry 17, no. 7 (October 9, 2020): 795–804. http://dx.doi.org/10.2174/1570193x16666191014164246.

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Faujasite Y zeolites, due to their outstanding properties, have numerous applications in the chemical industries like petroleum refining, adsorption, FCC, petrochemical, aromatic alkylation, natural gas dehydration, separation, and environmental protection. The astonishing properties include high surface area, high porosity, high thermal stability and large ion-exchange capacity. In this review study, a summary of different synthesis techniques of this type of zeolite has been addressed. Different kinds of techniques like seeding, free template, organic template, increasing the alkali treatment and temperature control methods are described. Subsequently, because of its important role as a catalyst for different processes, the application of this zeolite was reviewed for different chemical processes.

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43

Beard, Adrian, Krishnat P. Naikwadi, and Francis W. Karasek. "Formation of polychlorinated dibenzofurans by chlorination and de novo reactions with ferric chloride in petroleum refining processes." Environmental Science & Technology 27, no. 8 (August 1993): 1505–11. http://dx.doi.org/10.1021/es00045a003.

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44

Dzhashitov, Z. A., L. Ya Vlasenko, A. I. Samokhvalov, and L. N. Shabalina. "Influence of processing characteristics of crude oil on increasing the efficiency of petroleum refining." Chemistry and Technology of Fuels and Oils 21, no. 7 (July 1985): 333–36. http://dx.doi.org/10.1007/bf00723837.

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45

Kapustin, Vladimir, Elena Chernysheva, Alexandra Maximova, and Yulia Zinchenko. "Development of new catalytic processes for processing petroleum feedstock." Pure and Applied Chemistry 89, no. 10 (September 26, 2017): 1579–85. http://dx.doi.org/10.1515/pac-2016-1122.

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AbstractCurrently such factors as the use of heavier feedstocks, permanent strengthening of requirements to oil and gas product quality, introduction of technical regulations for oil products, which, in turn, necessitate the development of new technologies and catalysts, have a great influence on the global oil-refining and petrochemical industry development. Recently, a special attention is given to the development of new catalysts and processes for producing middle distillate fuels suitable for cold and arctic climatic conditions. Catalytic hydrodewaxing and isodewaxing processes are the most efficient in this field. Research into controlling a functional structure of catalysts and creation of catalytic systems based on zirconium dioxide modified by tungstate anions are of outstanding interest. The trend of the use of heavier petroleum feedstocks and the need to improve the oil conversion level demand will be based on destruction of high-molecular-weight compound structures with producing light and middle cuts. So, the most important processes for heavy oil residue conversion are those enabling to control transformations of resinous-asphaltenic materials by using nanoscale catalytic systems. One of the examples of the industrial implementation of technologies using suspended catalysts is the hydroconversion process implemented currently at AO TANECO (lisencer: TIPS RAS; general designer: OAO VNIPIneft).

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Raia, J. C., D. C. Villalanti, M. Subramanian, and B. Williams. "Application of High-Temperature Simulated Distillation to the Residuum Oil Supercritical Extraction Process in Petroleum Refining." Journal of Chromatographic Science 38, no. 1 (January 1, 2000): 1–5. http://dx.doi.org/10.1093/chromsci/38.1.1.

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Polichtchouk, Yuri M., and Irina G. Yashchenko. "Spatial Variability of Chemical Composition of Eurasian Oils." Eurasian Chemico-Technological Journal 4, no. 1 (June 29, 2017): 45. http://dx.doi.org/10.18321/ectj516.

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The study of relationships governing the variability of chemical composition of the Eurasian oils has been carried out on the basis of the statistical processing of the data on contents of total sulfur, resins,<br />paraffin wax and asphaltenes in oils. These indices are considered as the principal chemicals of oils chemical composition. The data processed for Eurasian continent was chosen from database on petroleum chemistry, which is create by Institute of Petroleum Chemistry of Siberian Branch of Russian Academy of Sciences and nowadays includes more than 9,000 entries of oil physical-chemical data on all main world oil-bearing basins. Latitudinal and longitudinal dependencies of the above indices of oils chemical composition were studied by methods of statistical and cluster analyses and means of geographical information system (GIS) ArcView 3.1. The results of these studies are represented on the computer maps. It is shown that properties of oils are statistically inhomogeneous in Eurasia depending on geographic position. In average, contents of total sulfur, resins and asphaltenes in crude oil increase in direction from<br />east to west. But the analysis doesn’t reveal longitudinal dependence of paraffin content, only a latitudinal dependence. In average, paraffin wax content in oils increases in direction from north to south. From the<br />analysis of the results of geozoning of oil-bearing territories using the whole complex of indices, the zones of oils that are homogenous by their properties was revealed. The results obtained may be used to solve the<br />problems of a rational use of hydrocarbon resources, in particular:<br />a) siting the oil-refining and petrochemical enterprises, b) developing the regional nets of a rational transporting of hydrocarbons and petroleum products.

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Ma, Tianqi, Shaohui Guo, Zhihui Guo, Qiushi Zhu, and Jinfu Chen. "Optimization of the real-time control strategy in petroleum-refining catalyst production wastewater treatment with shortcut nitrification." RSC Advances 5, no. 105 (2015): 86490–96. http://dx.doi.org/10.1039/c5ra14611a.

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Liu, Zhipeng, Quanyong Wang, Bei Zhang, Tao Wu, and Yujiang Li. "Efficient Removal of Bisphenol A Using Nitrogen-Doped Graphene-Like Plates from Green Petroleum Coke." Molecules 25, no. 15 (August 3, 2020): 3543. http://dx.doi.org/10.3390/molecules25153543.

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Green petroleum coke, a form of industrial waste produced in the oil-refining process, was used to synthesize nitrogen-doped graphene-like plates (N-GLPs) together with melamine. In this study, characterization and batch experiments were performed to elucidate the interaction mechanism of N-GLPs and bisphenol A (BPA). Structural analysis of N-GLPs, including scanning electron microscopy (SEM), X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FT-IR), Brunauer-Emmett-Teller (BET), and X-ray photoelectron spectroscopy (XPS), showed an obvious graphene-like structure and successful nitrogen doping. In addition, compared with 8.0 m2/g for green petroleum coke, the BET surface area of N-GLPs markedly increased to 96.6 m2/g. The influences of various factors, including contact time, temperature, and initial pH on BPA removal efficiency were investigated. It was found that 92.0% of BPA was successfully removed by N-GLPs at 50 °C. Based on the adsorption experiments, it was shown that electrostatic attraction, hydrogen bonding, and π-π interaction enhanced the adsorption capacity of N-GLPs for BPA. According to the thermodynamic data, the adsorption process was spontaneous, physical, and endothermic in nature. Therefore, N-GLPs are efficient adsorbent material to remove BPA from wastewater.

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Pangamol, Pathompong, Chakrit Sirisinha, Yongfeng Hu, and Stephen G. Urquhart. "Effectiveness of By-product Sulfur from Petroleum Refining as a Rubber Vulcanizing Agent: A XANES Investigation." Industrial & Engineering Chemistry Research 52, no. 48 (November 21, 2013): 17179–83. http://dx.doi.org/10.1021/ie4031456.

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