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Petroleum chemical complexity

Cold Hydrogenation A process for selectively hydrogenating petroleum fractions made by steam-reforming, in order to produce gasoline. Developed by Bayer and now in use in 70 refineries and chemical complexes worldwide. [Pg.69]

In the chemical and petroleum industries, the term cracking is used to describe a chemically complex process in which the decomposition of larger hydrocarbon molecules into smaller fragments plays a dominant role but is accompanied by a number of other reactions (isomerisation, cyclisation, polymerisation, disproportionation etc.). In this section, under catalytic cracking, only the primary fission of a C—C bond, which yields an alkene and a fragment with a C—H bond in the place of the former C—C bond... [Pg.309]

Phillips Petroleum Company, A Report on the Houston Chemical Complex Accident, Phillips Petroleum Company, Bartlesville, OK, 1990. [Pg.122]

K-Resin SBC was invented by Alonzo Kitchen, a research chemist at Phillips Petroleum Research and Development laboratories. With inventorship came the opportunity to name the new resin, which he called K-Resin . The first pilot plant resins were made in 1967, and commercial samples were prepared for test marketing in 1968. Commercial production started in October of 1972 at the SBC plant in Borger, Texas, on a 10 million pound per year capacity line. Initially, the solution product was steam stripped to remove the hydrocarbon solvent, but this left a significant haze in the resin. The finishing system was quickly converted to a devolatilizing extruder. Commercial production continued at this plant until 1979, ending with the opening of a new production facility at Adams Terminal (later renamed the Houston Chemical Complex) in Pasadena, Texas. The new plant had a nameplate capacity of 120 million pounds per year. Plant expansions increased the production capacity in 1988 and 1994 to a total nameplate capacity around 300 million pounds per year. [Pg.502]

Over the past few years, established analytical chemical methodology for crude oil and refined petroleum derivatives has been extended to the rapidly expanding field of coal liquefaction products and has assisted in the substantive reappraisal of such potential liquid fuel sources as oil shale, tar sands, and similar bitumenous deposits. While many of the analytical problems of separation, identification, and characterization are common to all of these fields, each area exhibits distinct requirements calling for specific development of appropriate methodology. Indeed, the added chemical complexity of the nonpetroleum-based liquid fuel sources presents many novel challenges to the chemical investigator. [Pg.348]

Methods of separation of hydrocarbons became more diversified. Fractional distillation was improved by the use of azeotropic and extractive distillation. Continuous adsorption on solids such as active charcoal or silica gel was established. Liquid-hquid solvent extraction, already used in petroleum refining, was adapted to the concentration and purification of some of the raw materials for petroleum chemicals finally, the formation of physical complexes, the so-called clathrate compounds, which permit separation of hydrocarbons of different shapes, is being developed as a new separation method, now known as extractive crystalhzation. [Pg.323]

Crude petroleum contains complex mixtures of hydrocarbons as well as relatively small amounts of nitrogen-, sulfur-, and oxygen-containing organic compounds, asphaltenes, and various trace metals (uncomplexed and complexed forms). The hydrocarbons can be divided into two classes related to their chemical structure the alkanes (normal, branched, and cyclo) and aromatic compounds (mono-, di-, and poly-, i.e., PAH). [Pg.102]

The molar flow rate of the supply of constituent j to the unit 0 CR) will be called F j and the molar flow rate of constituent j leaving the separation unit (j R CR, P, CP, BP) will be called Fj. In the petroleum chemical industry, chemically complex reactants are used (naphtha, LPG. ..), and it is much more common to carry out mass balances. Wqj and Wj are the mass-flows of constituent j supplying the process and leaving the separation unit, respectively. [Pg.70]

Phillips Petroleum Company. A report on the houston chemical complex accident Bartlesville, OK Phillips Petroleum Company 1990. [Pg.206]

A petrochemical complex (a specific kind of chemical complex) is generally a large facility that may encompass more than one company. The complex may process upstream petroleum products (primarily oil and natural gas) into complex downstream chemical and plastic products. As an illustration, a product flowchart (Fig. C-22) from the Petrochemical Company of Singapore (PCS), indicating numerous downstream companies, is included. The large number of companies and products resulting from the complex should be noted. (AU acron5uns used... [Pg.167]

The complexity of petroleum products raises the question of sample validity is the sample representative of the total flow The problem becomes that much more difficult when dealing with samples of heavy materials or samples coming from separations. The diverse chemical families in a petroleum cut can have very different physical characteristics and the homogeneous nature of the cut is often due to the delicate equilibrium between its components. The equilibrium can be upset by extraction or by addition of certain materials as in the case of the precipitation of asphaltenes by light paraffins. [Pg.28]

The dominant role of petroleum in the chemical industry worldwide is reflected in the landscapes of, for example, the Ruhr Valley in Germany and the U.S. Texas/Louisiana Gulf Coast, where petrochemical plants coimected by extensive and complex pipeline systems dot the countryside. Any movement to a different feedstock would require replacement not only of the chemical plants themselves, but of the expensive infrastmcture which has been built over the last half of the twentieth century. Moreover, because petroleum is a Hquid which can easily be pumped, change to any of the soHd potential feedstocks (like coal and biomass) would require drastic changes in feedstock handling systems. [Pg.366]

Other Specialty Chemicals. In fuel-ceU technology, nickel oxide cathodes have been demonstrated for the conversion of synthesis gas and the generation of electricity (199) (see Fuel cells). Nickel salts have been proposed as additions to water-flood tertiary cmde-oil recovery systems (see Petroleum, ENHANCED oil recovery). The salt forms nickel sulfide, which is an oxidation catalyst for H2S, and provides corrosion protection for downweU equipment. Sulfur-containing nickel complexes have been used to limit the oxidative deterioration of solvent-refined mineral oils (200). [Pg.15]

Step 4 deals with physical and chemical properties of compounds and mixtures. Accurate physical and chemical properties ate essential to achieve accurate simulation results. Most simulators have a method of maintaining tables of these properties as well as computet routines for calculations for the properties by different methods. At times these features of simulators make them suitable or not suitable for a particular problem. The various simulators differ ia the number of compounds ia the data base number of methods for estimating unknown properties petroleum fractions characterized electrolyte properties handled biochemical materials present abiUty to handle polymers and other complex materials and the soflds, metals, and alloys handled. [Pg.73]

A modem petroleum refinery is a complex system of chemical and physical operations. The cmde oil is first separated by distillahon into fractions such as gasoline, kerosene, and fuel oil. Some of the distillate fractions are converted to more valuable products by cracking, polymerization, or reforming. The products are treated to remove undesirable components, such as sulfur, and then blended to meet the final product specifications. A detailed analysis of the entire petroleum production process, including emissions and controls, is obviously well beyond the scope of this text. [Pg.518]

Risk-based decision making and risk-based corrective action arc decision making processes for assessing and responding to a health hazard. The processes take into account effects on human healdi and the enviroiunent, inasmuch as chemical releases vaiy greatly in terms of complexity, physical and chemical characteristics, and in the risk that they may pose. Risk-based corrective action (RBCA) was initially designed by the American Society for Testing and Materials (ASTM) to assess petroleum releases, but tlie process may be tailored for use with any hazard. [Pg.408]

The natural world is one of eomplex mixtures petroleum may eontain 10 -10 eomponents, while it has been estimated that there are at least 150 000 different proteins in the human body. The separation methods necessary to cope with complexity of this kind are based on chromatography and electrophoresis, and it could be said that separation has been the science of the 20th century (1, 2). Indeed, separation science spans the century almost exactly. In the early 1900s, organic and natural product chemistry was dominated by synthesis and by structure determination by degradation, chemical reactions and elemental analysis distillation, liquid extraction, and especially crystallization were the separation methods available to organic chemists. [Pg.3]

The fact that we have peaks within a 2D space implies that where no peak is found represents a true detector baseline or electronic noise level. In a conventional petroleum sample, a complex unresolved mixture response causes an apparent detector baseline rise and fall throughout the GC trace. It is probably a fact that in this case the true electronic baseline is never obtained. We have instead a chemical baseline comprising small response to many overlapping components. This immediately suggests that we should have more confidence in peak area measurements in the GC X GC experiment. [Pg.92]

On the fuel side, the issues are even more complex. Hydrogen, although currently it is made in relatively large amounts inside oil refineries for upgrading petroleum products and for making many bulk chemicals (e.g., ammonia), it is not currently distributed like conventional fuels. [Pg.525]

These are semisolid or solid substances formed in nature from crude oils after the volatile components have evaporated and the remainder has undergone oxidation and polymerization. They are also referred to as bitumens, waxes, and pitch. These materials are believed to consist of mixtures of complex organic molecules of high molecular weight. As with crude oils, which contain thousands of different chemical compounds, an exact chemical analysis for identification and composition is impractical to perform on the solid deposits of petroleum. [Pg.300]


See other pages where Petroleum chemical complexity is mentioned: [Pg.125]    [Pg.126]    [Pg.125]    [Pg.117]    [Pg.16]    [Pg.119]    [Pg.32]    [Pg.117]    [Pg.126]    [Pg.21]    [Pg.325]    [Pg.285]    [Pg.427]    [Pg.306]    [Pg.254]    [Pg.161]    [Pg.366]    [Pg.158]    [Pg.164]    [Pg.46]    [Pg.291]    [Pg.640]    [Pg.741]    [Pg.1324]    [Pg.34]    [Pg.125]    [Pg.379]   
See also in sourсe #XX -- [ Pg.24 ]




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