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Separation petroleum crudes

Petroleum crude oil, gas condensate, and natural gas are generally complex mixtures of various hydrocarbons and nonhydrocarbons with diverse molecular weights. In order to analyze the contents of a petroleum fluid it is a general practice to separate it first into five basic fractions namely, volatiles, saturates, aromatics, resins, and asphaltenes [74, 77]. Volatiles consist of the low-boiling... [Pg.224]

The separation of coal liquids by gel permeation chromatography using lOOA Styragel columns and solvents such as THF and toluene has been reported elsewhere (7.8.9.13.14). Coal liquids and petroleum crude are similar in their physical appearance as well as the complexity in composition. The major difference between the two is that petroleum crude does not contain oxygenated compounds, such as alkylated phenols, in substantial quantity. In addition, the average linear molecular size of petroleum derived asphaltenes (15.16) is much larger than that of coal derived asphaltenes (. ... [Pg.261]

Petroleum crude and its refinery products have two major component based on distillation. The portion that can be distilled under refinery conditions can be called volatiles and the nondistillables are the nonvolatiles. The volatiles can be analyzed by GC or GC-MS. The crude has both components. The distillate as the names applied, such as naphtha and kerosene contain only volatiles. When GPC is used for analyzing various distillates, the fractions separated by GPC can be characterized by GC or GC-MS. These data can be used to verify the nature of components present in various distillation cuts as a function of GPC elution volume. If the samples such as crude contains both volatiles as well as nonvolatiles, the samples should be separated into volatiles and nonvolatiles. The GPC of both components should be used to calibrate the GPC of the total crude. The parameter that can be obtained from GPC is effective molecular length. It can be used to relate other molecular parameters of interest after calibration. [Pg.263]

The GPC of a local crude (Bryan, Texas) sample spiked with a known mixture of n-alkanes and aromatics is shown in Figure 5 and the GPC of the crude is shown in Figure 6. The hydrocarbon mixture is used to calibrate the length of the species which separates as a function of retention volume. Ttie molecular length is expressed as n-alkane carboa units although n-alkanes represent only a fraction of the hydrocarbons in the crude. In addition to n-alkanes, petroleum crude is composed of major classes of hydrocarbons such as branched and cyclic alkanes, branched and cyclic olefins and various aromatics and nonvolatiles namely asphaltenes. Almost all of the known aromatics without side chains elute after n-hexane (Cg). If the aromatics have long side chains, the linear molecular size increases and the retention volume is reduced. Cyclic alkanes have retention volumes similar to those of aromatics. GPC separates crude on the basis of linear molecular size and the species are spread over 10 to 20 ml retention volume range and almost all of the species are smaller than the polystyrene standard (37A). In other words, the crude has very little asphaltenes. The linear... [Pg.263]

Elemental sulfur also is recovered as a by-product in processing natural gas and petroleum. Refining operations of natural gas and petroleum crude produce hydrogen sulfide, which also may occur naturally. Hydrogen sulfide is separated from hydrocarbon gases by absorption in an aqueous solution of alkaline solvent such as monoethanol amine. Hydrogen sulfide is concentrated in this solvent and gas is stripped out and oxidized by air at high temperature in the presence of a catalyst (Claus process). [Pg.892]

Coal liquids, petroleum crudes, and their distillation cuts have been separated into four or five fractions by SEC (5 15). The SEC fractions were analyzed by use of GC. The procedure was performed manually. It was inefficient, and susceptible to human error. The automated fraction collection followed by injection of the fraction into the GC reduces analysis time, and offers an option for collection of the desired number of fractions at predetermined time intervals. The manual collection of up to 10 one-ml fractions is also used in order to study the effectiveness of the automated method. [Pg.184]

Analytical separation and spectroscopic techniques normally used for petroleum crudes and residues were modified and used to characterize coal liquids, tar sands bitumens, and shale oils. These techniques include solvent extraction, adsorption, ion-exchange, and metal complexing chromatography to provide discrete fractions. The fractions are characterized by various physical and spectroscopic methods such as GLC, MS, NMR, etc. The methods are relatively fast, require only a few grams of sample, provide compound type fractions for detailed characterization, and provide comparative compositional profiles for natural and synthetic fuels. Additional analytical methods are needed in some areas. [Pg.33]

Experience has shown that to obtain meaningful results in analyzing petroleum crudes and residues, it is necessary to separate a sample into a certain number of well-defined fractions and to analyze these fractions in detail. Conclusions as to the composition of the original sample are then made by combining the results of the analyses on each fraction in a manner consistent with the steps performed to obtain them. This same approach is used for the synthetic liquid fuels, and this paper reports our results obtained on such materials. [Pg.33]

Separation Into Fractions. The separation procedure, developed for petroleum crudes and residues (40) is illustrated in Figure 1. This procedure is applicable to samples having a boiling point higher than 470° F. [Pg.35]

Distillation was the first method by which petroleum was refined, but this was not so much a refining method as a method for separation of the crude oil into fractions, such as kerosene, for which there was a demand and hence a ready market. Nevertheless, as petroleum refineries have evolved into present-day complexes, distillation units may still find a place, depending upon the characteristics of the crude oil feedstock, in a refinery sequence. A multitude of separations is accomplished by distillation, but its most important and primary function in the refinery is its use for the separation of crude oil into component fractions (Table 7-2) (Speight, 1999). [Pg.269]

Well over 50 large-scale EO model-based RTO applications have been deployed for petroleum refining processes. These model applications have been deployed in petroleum refineries Liporace et al., 2009 Camolesi et al., 2008 Mudt et al., 1995, both on separation units (crude atmospheric and vacuum distillation units) and on reactor units (including fluidized catalytic crackers (FCC), gasoline reformers, and hydrocrackers). [Pg.134]

For many years benzene (benzol) was made from coal tar, but new processes that consist of catalytic reforming of naphtha and hydrodealkylation of toluene are more appropriate. Benzene is a natural component of petroleum, but it cannot be separated from crude oil by simple distillation because of azeotrope formation with various other hydrocarbons. Recovery is more economical if the petroleum fraction is subjected to a thermal or catalytic process that increases the concentration of benzene. [Pg.75]

Organometallics have been identified in coals via very tedious separation procedures similar to those used for their isolation from petroleum samples (12). The difficulties associated with such schemes for the characterization of organometallics in coal are far greater than those associated with similar studies of petroleum crudes. This increase in difficulty is primarily due to the insolubility of the sample. Unfortunately most methods for increasing the solubility of coal are chemically of such severity that they would simultaneously decompose any organometallic that was originally present. [Pg.242]

Distillation is a unit operation that separates by vaporization liquid mixtures of miscible and volatile substances into individual components or groups of components. The separation of water and alcohol into the respective components of liquid air into nitrogen, oxygen, and argon and the separation of crude petroleum into gasoline, oil, and kerosene are examples of the distillation unit operation. [Pg.434]

Experience in class separations and analyses of fossil-derived materials began with the petroleum industry. The literature in this area is far too extensive to review here. Furthermore, petroleum literature deals principally with physical and chemical analyses of distillate fractions which are important to product characteristics. Recently, asphalts have received increased attention since they contain a wide range of known hazardous compounds. Most methods applied to whole samples of petroleum crudes have proven inadequate when dealing with synthetic coal liquids or shale oils because of stable emulsion formation in separation steps caused by larger amounts of inorganic and hydrophilic compounds. [Pg.283]

In the petroleum industry, the method of fractional distillation, differential distillation, or rectification is utilized for the primary separation of crude oil into fractions with regard to their boiling temperatures, because simple distillation is not efficient for separating liquids whose boiling points lie close to one another. [Pg.235]

Rectification units in the petroleum industry are used to separate the crude oil into fractions for subsequent processing in secondary processes such as catalytic reforming, cracking, alkylation, or coking. In turn, each of these complex secondary-processing units incorporates a fractional distillation tower to separate its own reaction products. [Pg.248]

A fractional distillation column for separating the components of petroleum crude oil. As the hot vapor moves upward, it condenses and the various components of the crude oil are separated according to their boiling points and ore drawn off as shown. [Pg.963]

In Table 17-1 are listed seven of the more important types of chemical structures according to which the non-petroleum liquids discussed in this chapter may be classified. All of these lubricants are synthetic l.t. their structures are the result of substantial chemical alteration of the starting material, in contradistinction to the refining of natural petroleum oils, which principally separates the crude oil into fractions and removes the unwanted portions thereof. Even though synthetic lubricants of the hydrocarbon type may have had their origin in raw materials obtained from petroleum, they are the products of substantial... [Pg.501]

Figure 1. Standardized separation scheme for petroleum crudes... Figure 1. Standardized separation scheme for petroleum crudes...
Hydrogen bromide is led rapidly into a glycol, HO(CH2) OH, at 100° to saturation and then slowly for a further 6 h at 135°. After cooling, the lower aqueous phase is separated benzene, light petroleum, or ether may be added as diluent to improve separation. The crude dibromide is washed with an equal volume of warm water, then in small portions with 10%... [Pg.219]


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See also in sourсe #XX -- [ Pg.26 , Pg.27 , Pg.28 ]




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Petroleum separation

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