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Vol 58, No 1 (2018)

Article

Physicochemical aspects of primary oil processing technology (Review)

Glagoleva O.F., Kapustin V.M.

Abstract

The review presents theoretical concepts of petroleum disperse systems, options for controlling phase transitions, balances of intermolecular interaction forces, and means to achieve the active state of feedstock through various kinds of its treatment so as practical ways to optimize technological processes can be found. These principles are described in relation to the primary processing of crude oil, namely, the demulsification and straight-run distillation processes.

Petroleum Chemistry. 2018;58(1):1-7
pages 1-7 views

Genesis of higher petroleum alkyltoluenes

Ostroukhov S.B.

Abstract

The genesis of higher alkyltoluenes with a normal alkyl chain (n-ATs) has been studied. The conditions for their formation from both individual C18 (oleic and stearic) fatty acids and C14 alcohol in the thermocatalytic mode and from Tasmanites planktonic algae during noncatalytic thermal treatment have been considered. The feasibility of the formation of n-ATs has been confirmed by determining their composition and structure.

Petroleum Chemistry. 2018;58(1):8-12
pages 8-12 views

Oxidative dehydrogenation of propane over vanadium catalyst supported on nano-HZSM-5

Varzaneh A.Z., Moghaddam M.S., Darian J.T.

Abstract

Vanadium catalyst supported on nano-HZSM-5 was utilized in oxidative dehydrogenation of propane to propylene. The physicochemical properties of the elaborated catalysts were investigated by means of XRD, SEM, FTIR spectra, UV-vis, Raman, NH3-TPD and H2-TPR techniques. The effect of vanadium loading (2–10 wt %), temperature (500–600°C) and oxygen to propane ratio (0.5–1.5) on conversion, propylene and ethylene selectivity was studied using full factorial design of experiments. The obtained data were statistically analyzed using the Analysis of Variance (ANOVA) and a p < 0.05 was considered statistically significant. The mathematical relationship of conversion, propylene and ethylene selectivity on three independent variables approximated by a second-order quadratic model. Two-dimensional contour plots were drawn to investigate the effect of independent variables and their interaction on the chosen responses. The function of temperature, oxygen to propane ratio and vanadium content such as acidity and reducibility on the performance of supported vanadium catalysts were discussed.

Petroleum Chemistry. 2018;58(1):13-21
pages 13-21 views

Promoted catalysts for hydrogenation of bicyclic aromatic hydrocarbons obtained in situ from molybdenum and tungsten carbonyls

Zakharyan E.M., Onishchenko M.I., Maksimov A.L.

Abstract

Promoted Мo and W catalysts have been prepared in situ via thermal decomposition of precursors, oil-soluble salts Mo(CO)6, W(CO)6, С°C16H30O4, and NiC16H30O4. TiO2, Al2O3, and ZrO(NO3)2 · 6H2O have been used as the acidic additives. Also, Mo and W unsupported sulfide catalysts have been prepared in the presence of elemental sulfur as the sulfiding agent. The catalysts have been characterized by transmission electron microscopy and X-ray photoelectron spectroscopy. The activity of the catalysts prepared in situ has been evaluated in the hydrogenation reaction of bicyclic aromatic hydrocarbons by the example of model mixtures of 10% solutions of naphthalenes (unsubstituted naphthalene, 1- and 2-methylnaphthalenes, and 1,5- and 2,3-dimethylnaphthalenes) in n-hexadecane. The effect of the precursor/acidic oxide ratio on the activity of the formed catalyst has been found. Hydrogenation of bicyclic aromatic hydrocarbons has been conducted at a hydrogen pressure of 2 and 5 MPa and a temperature of 380 and 400°C for 2 h. Hydrogenation of the unsubstituted aromatic ring has been preferable due to the absence of steric hindrances. The degree of conversion of n-hexadecane under the reaction conditions has been 1.5–7.5% depending on the reaction temperature. It has been found that the activity of the sulfided catalyst in the conversion of 1- and 2-methylnaphthalenes is inferior to the activity of the unsulfided analogue, while partial replacement of TiO2 by Al2O3 results in a decrease in the conversion of the substrates as opposed to the unsulfided catalysts, in which the use of nanocrystalline Al2O3 promotes an increase in the conversion.

Petroleum Chemistry. 2018;58(1):22-31
pages 22-31 views

Direct conversion of ethanol and fusel oils to alkane–aromatic hydrocarbons in the presence of a pilot Pd–Zn/TsVM catalyst

Chistyakov A.V., Tsodikov M.V., Chudakova M.V., Gubanov M.A., Zharova P.A., Bukina Z.M., Kolesnichenko N.V., Gekhman A.E., Khadzhiev S.N.

Abstract

The conversion of ethanol and fusel oils to a С3–С12 alkane–aromatic fraction with high activity and selectivity in the presence of the Pd–Zn/TsVM pilot catalyst has been demonstrated. It has been shown that the ethanol conversion to alkanes and aromatic hydrocarbons in the presence of this catalyst proceeds by various routes to give ethylene and diethyl ether as intermediate products providing a 90–95% yield on the converted ethanol carbon basis for the target С3–С12 fraction containing up to 40% of branched alkanes.

Petroleum Chemistry. 2018;58(1):32-42
pages 32-42 views

Partial oxidation of methane to synthesis gas: Novel catalysts based on neodymium–calcium cobaltate–nickelate complex oxides

Dedov A.G., Shlyakhtin O.A., Loktev A.S., Mazo G.N., Malyshev S.A., Tyumenova S.I., Baranchikov A.E., Moiseev I.I.

Abstract

Novel catalysts based on neodymium–calcium cobaltate–nickelate complex oxides for the partial oxidation of methane to synthesis gas have been synthesized and studied using catalyst precursors with the general formula NdCaCo1–xNixOn (x = 0, 0.2, 0.4, 0.6, 0.8, 1) prepared by the solid state synthesis method. It has been shown that the synthesized samples form a series of solid solutions with a K2NiF4 structure at x ≤ 0.8 or a rhombically distorted K2NiF4 structure at x = 1. The products of conversion of the resulting precursors in a methane–oxygen mixture at high temperatures have shown high methane conversions and synthesis gas yields. The highest values of these parameters have been achieved in the presence of catalysts synthesized by the reduction of NdCaCo0.4Ni0.6On and NdCaNiOn precursors. The complete replacement of cobalt with nickel has led to an increase in the synthesis gas yield; however, it has been found that the resulting catalyst is prone to carbonization. It has been determined that an optimum nickel to cobalt ratio in the catalyst composition provides the formation of a carbonization-resistant catalyst.

Petroleum Chemistry. 2018;58(1):43-47
pages 43-47 views

Hydrogenation of petroleum resins in the presence of supported sulfide catalysts

Petrukhina N.N., Zakharyan E.M., Korchagina S.A., Nagieva M.V., Maksimov A.L.

Abstract

The hydrogenation of petroleum resins (PRs) in the presence of commercial NVS-A, GO-15K, AGKD-400, and AKM nickel–tungsten, cobalt–molybdenum, and nickel–molybdenum sulfide catalysts and sulfided palladium MA-15 has been studied. Features of changes in the average molecular mass (M) of the PRs in the presence and absence of sulfur compounds in the reaction medium have been determined. The highest degree of hydrogenation is achieved in dilute PR solutions with a concentration of 10–20%; an increase in the process temperature and pressure leads to an intensification of the polymer chain degradation reactions. Swelling of the polymer globules in “good” solvents (benzene, toluene) makes the polymer chains more accessible to the active sites of the catalyst and thereby leads to an intensification of both the hydrogenation and thermal degradation reactions. The process run without any solvent does not provide a sufficient degree of hydrogenation of aromatic moieties owing to the high viscosity of the reaction mass and the resulting high diffusion restrictions.

Petroleum Chemistry. 2018;58(1):48-55
pages 48-55 views

Synthesis of raspberry ketone via Friedel-Crafts alkylation reaction catalyzed by sulfonic acid-functional ionic liquids

Wang W., He Z., Li C., You Z., Guo H.

Abstract

Phenol and butanolone catalyzed by different SO3H-functionalized ionic liquids (ILs) for synthesis of raspberry ketone (RK) had been investigated. The influences of different ionic liquids, reaction time, reaction temperature, reactant ratio, the amount of ionic liquid were investigated. The yield of raspberry ketone was 82.5% under the optimum reaction condition. In addition, the ILs (3-sulfo)propyltriamine bisulfate ([TEA-PS][HSO4]) can be recycled up to five consecutive times without loss of activity. This method had the advantages of mild conditions, high product yield, easy to separate from the product, as well as environmentally friendly procedure. At the same time, the possible reaction mechanism was discussed.

Petroleum Chemistry. 2018;58(1):56-61
pages 56-61 views

Steam reforming of dimethyl ether using a membrane-catalytic reactor

Fedotov A.S., Antonov D.O., Uvarov V.I., Tsodikov M.V., Khadzhiev S.N.

Abstract

It has been found that during the steam reforming of dimethyl ether into synthesis gas using a porous ceramic Ni–Co-containing membrane catalytic converter, an increased hydrogen yield with H2/CO = 15–20 is reached at T = 450–500°C. Reforming in a hybrid membrane reactor with a Pd–Ru alloy membrane integrated into the reaction volume provides recovery of ultrapure hydrogen up to 50% at a temperature of 500–700°C.

Petroleum Chemistry. 2018;58(1):62-67
pages 62-67 views

Study of the pyrolysis of solid organic polymers by their heating with metal melt

Ulyanov V.V., Koshelev M.M., Kharchuk S.E., Gulevskii V.A., Timochkin A.V.

Abstract

The kinetics of the pyrolysis of solid organic polymers by their heating with a gas or a metal melt have been studied. The design features of a small-sized pyrolysis unit for organic polymers have been determined. The pyrolysis process on this unit has been experimentally substantiated. The specifics of the processes of “conventional” pyrolysis in the gaseous heat carrier and the pyrolysis of organic polymers in a lead melt have been revealed. It has been shown that the resulting pyrolysis liquid can be used as a feedstock for the production of the expensive organic solvent limonene or synthetic oil similar in properties to domestic crude oil.

Petroleum Chemistry. 2018;58(1):68-75
pages 68-75 views

Enhancement of the Fischer–Tropsch process for producing long-chain hydrocarbons on a cobalt–alumina–silica gel catalyst

Savost’yanov A.P., Narochnyi G.B., Yakovenko R.E., Mitchenko S.A., Zubkov I.N.

Abstract

The effects of the H2/CO ratio, pressure, temperature, and the reaction-gas recycle ratio on the selectivity for hydrocarbons (HCs), including long-chain C35+ HCs, in the Fischer–Tropsch synthesis over a supported industrial cobalt–silica gel catalyst have been studied. The synthesis parameters have been as follows: a pressure of 2.0 or 6.0 MPa, an H2/CO ratio of 1–5, a recycle ratio of 2–6, a temperature of 150–240°C, and a gas hourly space velocity of 1000 h−1. It has been shown that gas recycling provides thermal stability in the catalyst bed, significantly increases the yield of C35+ HCs, and makes it possible to control the group and fractional composition of the synthesis products.

Petroleum Chemistry. 2018;58(1):76-84
pages 76-84 views

Synthesis of pour point depressant for heavy oil from waste organic glass

Chen G., Yuan W., Bai Y., Zhao W., Zhang J., Wu Y., Gu X., Chen S., Yu H.

Abstract

Polymethyl methacrylate (PMMA) is widely used as a substitute for glass, known as organic glass. During the processing and after use, there are amount of castoff. Based on the similar framework, PMMA could be useful feed stock to synthesis poly methacrylamide (PMAA) used for crude oil additive. In this work PMAA was prepared by aminolysis reaction of PMMA and aliphatic amines. The performance of PMAA on heavy oil was evaluated as pour point depressant as well as paraffin inhibiter. The highest pour point reduction depression was achieved as 12.1°С with the dosage of 600 ppm PMAA 1. Differential scanning calorimetry and paraffin crystal morphology studies were conducted to elucidate the mechanism of pour point reduction.

Petroleum Chemistry. 2018;58(1):85-88
pages 85-88 views

Determination of the most efficient form of sulfur for use as a natural rubber curing agent by comparison of physical and thermal attributes of cured rubber

Motavalizadehkakhky A., Shahrampour H.

Abstract

Vulcanization, by creating a three-dimensional cross-linked network, improves the physicalmechanical and thermal properties of elastomers. A popular agent for curing natural rubber (NR) is sulfur. Insoluble sulfur (IS) and rhombic sulfur (RS) are common allotropes of elemental sulfur. In this research, it was observed that the use of the two types of sulfur (IS and RS) gives different results. In terms of cure behavior, tear resistance and hardness, RS-vulcanized NR performed better, whereas in viscosity, tensile strength, aging and compression set, IS-vulcanized NR was better; because of the lack of blooming, IS could replace of rhombic sulfur as the curing agent in certain applications.

Petroleum Chemistry. 2018;58(1):89-93
pages 89-93 views

Thermo-responsive temporary plugging agent based on multiphase transitional supramolecular gel

Zhao L., Pei Y., Du G., Wen Z., Luo Z., Du J.

Abstract

In this study, a thermo-responsive temporary plugging agent was developed with the property of sol-gel-sol transition behavior at different temperatures. At low temperature, the material is in sol state, while increasing temperature led to a stable gel formation, but the gel can transform to sol again upon further heating. This unique behavior was characterized by a series of SEM, FT-IR, XRD, rheology and viscoelasticity measurements. All scientific results showed non-covalent interactions between the components, which play an important role for the supramolecular gel formation. These findings provide this system can be applied as temporary plugging agent by the idea of temperature-induced smart material with the specialty of cross-linker and gel-breaker free. Physical simulation experiment results showed that the material is good mobility liquid at room temperature. After injecting to formation, the fluid gradually transformed to hard gel around 90°C with sufficient strength to block cracks. Upon further heating by formation, the hard gel would collapse to sol around 110°C without adding additional gel breakers, leading to flowback sufficiently and low damage to fracture. This novel temporary plugging agent also has potential use in diverting fracturing, network fracturing, drilling, well completion, well clean etc.

Petroleum Chemistry. 2018;58(1):94-101
pages 94-101 views