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Petroleum distillation fractions

The equihbrium shown in equation 3 normally ties far to the left. Usually the water formed is removed by azeotropic distillation with excess alcohol or a suitable azeotroping solvent such as benzene, toluene, or various petroleum distillate fractions. The procedure used depends on the specific ester desired. Preparation of methyl borate and ethyl borate is compHcated by the formation of low boiling azeotropes (Table 1) which are the lowest boiling constituents in these systems. Consequently, the ester—alcohol azeotrope must be prepared and then separated in another step. Some of the methods that have been used to separate methyl borate from the azeotrope are extraction with sulfuric acid and distillation of the enriched phase (18), treatment with calcium chloride or lithium chloride (19,20), washing with a hydrocarbon and distillation (21), fractional distillation at 709 kPa (7 atmospheres) (22), and addition of a third component that will form a low boiling methanol azeotrope (23). [Pg.214]

Blackburn GR, Deitch RA, Schreiner CA, et al. 1986. Predicting carcinogenicity of petroleum distillation fractions using a modified Salmonella mutagenicity assay. Cell Biol Toxicol 2 63-84. [Pg.167]

Cold-Water Process. The cold-water bitumen separation process has been developed to the point of small-scale continuous pilot plants. The process uses a combination of cold water and solvent. The first step usually involves disintegration of the tar sand charge, which is mixed with water, diluent, and reagents. The diluent may be a petroleum distillate fraction such as kerosene and is added in a ca 1 1 weight ratio to the bitumen in the feed. The pH is maintained at 9-9.5 by addition of wetting agents and ca 0.77 kg of soda ash per ton of tar sand. The effluent is mixed with more water, and in a raked classifier the sand is settled from the bulk of the remaining mixture. The water and oil overflow the classifier and are passed to thickeners, where the oil is concentrated. Clay in the tar sand feed forms emulsions that are hard to break and are wasted with the underflow from the thickeners. [Pg.359]

Occupational standards for JP-8 are primarily based on knowledge about the toxicity of kerosene and naphtha (a petroleum distillate fraction). National Institute for Occupational Safety and Health (NIOSH) guidelines include an 8-hour (hr) time-weighted-average recommended exposure limit (TWA-REL) for naphtha of 400 milligrams per cubic meter (mg/m3) (100 parts per million (ppm)) (NIOSH... [Pg.145]

Derivatives of 6,7-dihydro-5//-1 -pyrindine (10) comprise the largest group of 1-pyrindines. Studies of the basic nitrogen compounds in the 120°-375° petroleum distillate fractions via chemical reactivity and infrared, mass, ultraviolet, and proton magnetic resonance spectrometry have led to the separation and identification of many derivatives of 10 2> 3> 5 8,56-66... [Pg.202]

Direct solvent extraction is the most widely used oil-recovery method for soybeans, but it also requires considerable capital and large scale to compete. In actual practice, solvent extraction is used to crush over 98% of the soybean processed in the United States. Process flow diagrams are shown in Figures 3 and 4. Most soybean solvent-extraction plants process more than 2,500 MT/day (Figure 5), and some are capable of processing as much as 5,000 MT/day (especially newly constructed plants in Brazil). Direct-solvent-extraction plants smaller than 1,000 MT/day have difficulty competing in the United States. At various times, soybeans have been extracted commercially with petroleum distillate fractions that resemble gasoline, acetone, carbon disulfide, ethanol, trichloroethylene, and even water. [Pg.1228]

Thus, the term petroleum distillates may be used genetically and interchangeably for two or three different types of petroleum distillation fractions. It can be confusing in that many commercial products will list the term as an ingredient even though it does not contain petroleum naphtha (e.g., the label of a solvent may say contains petroleum distillates simply because some of the components were derived from crude oil). [Pg.1957]

Lubricants have been used by mankind from the very early days of civilization to assist in reducing the energy needed to slide one object against another. The first lubricants were animal fats, and much later whale oil was used. It was not until crude oil was discovered in commercial quantities in Oil Springs, Ontario, Canada, in 1858 and in Titusville, Pennsylvania, in the United States in 1859 that the concept of petroleum-based lubricants could be seriously considered on a large scale. The first petroleum refinery to produce base stocks (the petroleum distillates fractions used in lubricants) in the Western Hemisphere was built by Samuel Weir in Pittsburgh in the 1850s. One of the earliest lubricant producers (to reduce waste production) was the Standard Works in Cleveland, Ohio, owned in part by John D. Rockefeller, whose company subsequently became Standard Oil. [Pg.1]

Special boiling point hydrocarbons are used for quick-drying paints, dipping solutions, and quick-drying adhesives. Their flash point is below 21 C, which means that they must be used in explosion-proof areas. Petroleum ether is a special petroleum distillation fraction (hp 40-60 C). and is used as a solvent in the chemical industry. [Pg.327]

Many of the commonly known solvents are aetually petroleum distillation fractions and are eomposed of a number of compounds (e.g., mineral spirits and naphthas). There are two general types of solvents derived from petroleum, aliphatics or aromatics. Aromatics are stronger solvents than aliphatics since they dissolve a wider variety of resins. Most major solvent suppliers (chemical manufacturers) produee several types and variations of these solvents and the associated HAP contents can vary significantly from manufacturer to man-ufaeturer and from batch to batch. These types of solvents are used extensively and are present in the majority of marine coatings. Table 14.26.4 provides a summary of common petroleum distillate solvents and solvent blends and their associated HAP content. For any... [Pg.1033]

Soluble in water and in polar and non-polar solvents, e.g. in petroleum distillate fractions (naphtha), kerosene, gas oil, mineral oils, propane, butane, toluene, xylenes, halogenated hydrocarbons... [Pg.104]

Petroleum distillate fractionators are identical in appearance to the classical model studied in the classroom. They are fitted with condensers and reboilers and process generally one feed into two or, at the most, three products. The feed enters the tower at an intermediate tray so that there is always a stripping section below the feed tray and a... [Pg.92]

Materials that are related through the sulfonate group include the aliphatic paraffin sulfonates produced by the photochemical sulfonation of rehnery hydrocarbons, petroleum sulfonates derived from selected petroleum distillate fractions, olehn sulfonates, A -acyl-A -alkyltaurines, sulfosuccinate esters and related compounds, alkylaryl sulfonates, and ligninsulfonates, which are a byproduct of the paper manufacturing process. While complete coverage of the class would be prohibitive, some of the most important types are described below. [Pg.55]


See other pages where Petroleum distillation fractions is mentioned: [Pg.187]    [Pg.359]    [Pg.365]    [Pg.285]    [Pg.453]    [Pg.454]    [Pg.1960]    [Pg.138]    [Pg.173]    [Pg.214]    [Pg.327]    [Pg.365]    [Pg.954]    [Pg.508]   
See also in sourсe #XX -- [ Pg.3 , Pg.238 , Pg.239 ]

See also in sourсe #XX -- [ Pg.3 , Pg.238 , Pg.239 ]




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