Acidity, also hydrocarbon

The term naphthenic acid, as commonly used in the petroleum industry, refers collectively to all of the carboxyUc acids present in cmde oil. Naphthenic acids [1338-24-5] are classified as monobasic carboxyUc acids of the general formula RCOOH, where R represents the naphthene moiety consisting of cyclopentane and cyclohexane derivatives. Naphthenic acids are composed predorninandy of aLkyl-substituted cycloaUphatic carboxyUc acids, with smaller amounts of acycHc aUphatic (paraffinic or fatty) acids. Aromatic, olefinic, hydroxy, and dibasic acids are considered to be minor components. Commercial naphthenic acids also contain varying amounts of unsaponifiable hydrocarbons, phenoHc compounds, sulfur compounds, and water. The complex mixture of acids is derived from straight-mn distillates of petroleum, mosdy from kerosene and diesel fractions (see Petroleum). 

Several solvent uses have been proposed. Dimethyl sulfate has been used as a solvent for the study of Lewis acid—aromatic hydrocarbon complexes (148). It also is effective as an extraction solvent to separate phosphoms haUde—hydrocarbon mixtures and aromatic hydrocarbons from aUphatics, and it acts as an electrolyte in electroplating iron (149—152). The toxicity of dimethyl sulfate precludes its use as a general-purpose solvent. 

Activated alumina and phosphoric acid on a suitable support have become the choices for an iadustrial process. Ziac oxide with alumina has also been claimed to be a good catalyst. The actual mechanism of dehydration is not known. In iadustrial production, the ethylene yield is 94 to 99% of the theoretical value depending on the processiag scheme. Traces of aldehyde, acids, higher hydrocarbons, and carbon oxides, as well as water, have to be removed. Fixed-bed processes developed at the beginning of this century have been commercialized in many countries, and small-scale industries are still in operation in Brazil and India. New fluid-bed processes have been developed to reduce the plant investment and operating costs (102,103). Commercially available processes include the Lummus processes (fixed and fluidized-bed processes), Halcon/Scientific Design process, NIKK/JGC process, and the Petrobras process. In all these processes, typical ethylene yield is between 94 and 99%. 

The problems with the combustion reaction occur because the process also produces many other products, most of which are termed air pollutants. These can be carbon monoxide, carbon dioxide, oxides of sulfur, oxides of nitrogen, smoke, fly ash, metals, metal oxides, metal salts, aldehydes, ketones, acids, polynuclear hydrocarbons, and many others. Only in the past few decades have combustion engineers become concerned about... 

In 1892, the chemist Schopf, in an attempt to prepare 2-phenylamino-3-naph-thoic acid, developed a synthetic route leading to the anilide of 2-hydroxy-3-naph-thoic acid. His method continues to be used today, if only in a slightly modified form. He added phosphorus trichloride to a molten reaction mixture containing aniline and 2-hydroxy-3-naphthoic acid (beta-oxynaphthoic acid, also known as BONA) and received Naphthol AS in good yield. Modern processes differ from this principle only in terms of reaction control the synthesis is now carried out in the presence of organic solvents, such as aromatic hydrocarbons. 

Alkali metal salts of carbojQ/ Uc acids also undergo decarbojqrlation on electrolysis of their aqueous solutions and form hydrocarbons having... 

Oeavage of esters to acids and hydrocarbons mentioned above was achieved not only with hydrides but also by catalytic hydrogenation and reduction with metals. For example the acetate of mandelic acid was converted to mandelic acid and acetic acid by hydrogenation at 20° and 1 atm over palladium on barium sulfate in ethanol in the presence of triethylamine in 10 minutes [1035], and a,a-diphenylphthalide was reduced by refluxing for 5 hours with zinc in formic acid to a,a-diphenyl-o-toluic acid in 92% yield [1036]. Such reductions are of immense importance in esters of benzyl-type alcohols where the yields of the acids are almost quantitative. 

The efficiency of the catalysis would also depend on the binding of the substrate to the piperazine-2,5-dione by means of weak forces. Imanishi and his group (85BCJ497) have sought to achieve this by means of hydrophobic interactions. They have chosen as substrates p-nitrophenyl esters of long-chain fatty acids the hydrocarbon chain would enter into... 

The amount of acid in the acid-hydrocarbon reaction mixture also has an important bearing on the alkylate quality. If the reaction mixture contains less than 40% acid by volume, an acid-in-hydrocarbon emulsion results. Above this 40% inversion point, a hydrocarbon-in-acid emulsion is formed. The latter type produces the better product and consequently an acid volume of 60 to 70% of the reaction mixture is normally maintained. 

As in sulfuric acid alkylation, the hydrocarbon-acid emulsion passes from the contactor into an acid settler for separation of acid and hydrocarbon phases and the acid layer recirculates to the reactor. Unlike sulfuric acid, however, hydrofluoric acid is appreciably soluble in hydrocarbons, and as much as 1% by weight may be retained in the hydrocarbon layer. The necessity of recovering this acid from the hydrocarbon phase results, in another difference between hydrofluoric and sulfuric acid processing in that a hydrofluoric acid stripper is required. This stripper is ordinarily packed with aluminum rings which serve not only as tower packing but also as a catalyst for the decomposition of organic fluorides into hydrocarbons and free hydrofluoric acid. 

Polymerization of isobutylene, in contrast, is the most characteristic example of all acid-catalyzed hydrocarbon polymerizations. Despite its hindered double bond, isobutylene is extremely reactive under any acidic conditions, which makes it an ideal monomer for cationic polymerization. While other alkenes usually can polymerize by several different propagation mechanisms (cationic, anionic, free radical, coordination), polyisobutylene can be prepared only via cationic polymerization. Acid-catalyzed polymerization of isobutylene is, therefore, the most thoroughly studied case. Other suitable monomers undergoing cationic polymerization are substituted styrene derivatives and conjugated dienes. Superacid-catalyzed alkane selfcondensation (see Section 5.1.2) and polymerization of strained cycloalkanes are also possible.118... 

The compounds formed are termed sulphones they are also formed by the action of cone, and fuming sulphuric acid on hydrocarbons (see p. 313), and by heating aromatic sulphonic acids with an aromatic hydrocarbon in presence of a dehydrating agent, such as P205. 

It will be shown below that with the aid of liquid ammonia solutions of potassium amide, the acidity of hydrocarbons (including even saturated ones) cannot only be detected but also determined quantitatively from measurements of hydrogen isotope exchange rates. 

The methylmalonyl-CoA unit, which is the precursor to methyl-branched fatty acids and hydrocarbons, arises from the carbon skeletons of valine and isoleucine, but not succinate (Dillwith et al., 1982). Propionate is also a precursor to methylmalonyl-CoA, and in the course of these studies, a novel pathway for... 

Oxybutyric Acid (CH3-CH(OH)-CH2-COOH).—From this acid were obtained in the positive electrolyte crotonic aldehyde and a little formic acid, also resinous substances. Considerable quantities of carbonic acid, also a little carbon monoxide and unsaturated hydrocarbons, are formed. The small quantities... 

Acetic Acid.—Besides hydrogen, carbon mon- and dioxides, Maquenne 3 also obtained methane, ethylene, and acetylene. With increasing pressure he found an increase in hydrogen and carbon monoxide, a decrease in-carbonic acid and hydrocarbons. Hemptinne observed similar results with his experimental arrangement. He accepts the following as the primary decomposition process, corresponding to that of the alcohols ... 

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