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Engineering aspects

To appreciate the engineering aspects of Powerforming, it would be helpful to go over some of the engineering design considerations. [Pg.52]

The Powerformer reaction absorbs heat it is largely an endothermic reaction. This heat of reaction is in the order of 200-350 BTU/pound, depending on the type of feed. Since the individual Powerforming fixed bed reactors operate [Pg.52]

The basic assumptions are as follows The precatalyst is first reduced to the zero-valent palladium species 4.42. Oxidative addition of Ar-Cl to 4.42 gives [Pg.77]

Finally, ArCOCl is reductively eliminated from 4.44. The acid chloride undergoes hydrolysis to give ibuprofen. Direct reaction between 4.44 and water to give 4.42, ibuprofen, and HC1 is also possible. [Pg.77]

A block diagram of the Monsanto process for acetic acid production is shown in Fig. 4.13. The process flow sheet is simple since the reaction conditions are mild (180°C/30-40 bar) when compared to the BASF process (250°C/700 bar). More than 40% of world s acetic acid is made by the Monsanto process. One of the problems with this process is the continuous loss of iodine. A block diagram of the Eastman process for acetic anhydride production is shown in Fig. 4.14. The process generates minimum waste, and all process tars are destroyed to recover iodine and rhodium. [Pg.77]

Carbon monoxide is first stripped off particulate matter in a cyclone separator or in a scrubber. Scrubbing also removes tar or heavy hydrocarbon fractions. Acidic gases, if present, are removed by absorption in monoethanol amine or in potassium carbonate. This pretreated gas is sent to the next section for further purification. Commercial processes for final purification are based on the absorption of carbon monoxide by salt solution, low-temperature condensation, or fractionation, or by pressure-swing adsorption using a solid material. [Pg.77]

The salt process employs scrubbing of the gas with cuprous ammonium salt solution. Carbon monoxide forms a complex with the solution at high pressure and low temperature in the absorption column. The absorbed pure carbon monoxide is released from the solution at low pressure and high temperature in the regenerator/stripper section. Any carbon monoxide that is liberated in the stripper section is removed by subsequently washing the gas with caustic. Sulfur has to be removed in the pretreatment stage to prevent the formation of solid sulfide. [Pg.77]

If promising experimental results with respect to reaction rate, selectivity and yield motivate the development of an industrial process based on a self-organised surfactant system [Pg.166]

Carbon monoxide free from impurities is required for all carbonylation reactions. The selection of the purification process depends on the level of impurity permitted, the source of gas that needs to be purified, etc. The source stream is in most cases a mix of CO ( 6-60%), CO ( 3-15%), nitrogen hydrogen, etc. Blast furnace gas predominantly has nitrogen (-60%), while coke oven, steam reforming, and water gases have hydrogen (-30-75%). Coke oven and water gases also have methane as an additional component (12-28%). [Pg.125]

In the cryogenic partial condensation process, the fed gas is cooled to -85°K, which condenses methane (BP 112 K) and much of the CO as it has high solubility in methane. Uncondensed hydrogen-rich gas is cooled further to -70 K to liquefy additional carbon monoxide (BP 81.5 K). In the liquid methane wash process, the hydrogen-rich stream is washed in a column with methane, which absorbs carbon monoxide and other gases. Carbon monoxide is recovered from this solution in a fractional distillation column. [Pg.125]

In PSA, a copper adsorbent is finely dispersed on a high-surface-area support such as alumina or carbon. During the adsorption cycle, carbon monoxide is selectively adsorbed from the gas mixture. During the depressurization cycle, carbon monoxide is desorbed from the solid matrix. [Pg.126]


A book that covers many engineering aspects of polymers. [Pg.2542]

L. V. CraHey and L. J. CraHey, In-Plant Practicesfor Job Related Health Ha ards Control, Vol. 2, Engineering Aspects, John Wiley Sons, Inc., New York, 1988. [Pg.110]

S. Hamilton, in Proc. of 2nd Sjmposium on Engineering Aspects of MHD, Columbia University Press, New York, 1962, pp. 211—227. [Pg.438]

J. Louis, "Studies on an Inert Gas Disk Hall Generator Driven in A Shock Tutmel," Proc. of 8th Sjmposium on Engineering Aspects of MHD, Stanford, Calif., Mat. 1967. [Pg.438]

E. Hals and co-workers, in Prof, of 20th Sjmposium on Engineering Aspects of MHD, Irving, Calif.,June 1982, pp. 1.1.1—1.1.9. [Pg.438]

R. E. Weinstein and R. B. Boulay, in Proc. ofi26th Sjmposium on Engineering Aspects ofiMHD, Nashville, Term., June 1988, pp. 8.5.1—8.5.9. [Pg.438]

J. Khnget and co-workers, in Proc. of 22nd Sjmposium on Engineering Aspects ofiMHD, Starkvihe, Miss., June 1984, pp. 10.2.1—10.2.20. [Pg.438]

L. W. Crawford and co-workers, "Nitrogen-Oxide Control in a Coal-Eked MHD System," Proc. of 21st Sjmposium on Engineering Aspects of MHD, suppl. vol., Argorme, HI., June 1983. [Pg.438]

Engineering Aspects of Hemodialysis. Engineering interest in hemodialysis is concentrated on the optimization of the hemodialysis membrane (4,41), the dependency of solute removal on membrane and device characteristics (14,15), and quantitation of hemodialysis therapy through urea pharmacokinetics (42—44). [Pg.34]

Engineering Aspects Trevan, M. D., Immobilized Enzymes An Introduc-... [Pg.2150]

Sundararajan, C. 1992. Structural Engineering Aspects of Plant Risk Assessment. [Pg.157]

Nitric acid is one of the three major acids of the modem chemical industiy and has been known as a corrosive solvent for metals since alchemical times in the thirteenth centuiy. " " It is now invariably made by the catalytic oxidation of ammonia under conditions which promote the formation of NO rather than the thermodynamically more favoured products N2 or N2O (p. 423). The NO is then further oxidized to NO2 and the gases absorbed in water to yield a concentrated aqueous solution of the acid. The vast scale of production requires the optimization of all the reaction conditions and present-day operations are based on the intricate interaction of fundamental thermodynamics, modem catalyst technology, advanced reactor design, and chemical engineering aspects of process control (see Panel). Production in the USA alone now exceeds 7 million tonnes annually, of which the greater part is used to produce nitrates for fertilizers, explosives and other purposes (see Panel). [Pg.465]

Ionic liquids operate in true biphasic mode. While the recovery and recyclability of ionic liquid was found to be more efficient than with the conventional AICI3 catalyst (red oil), the selectivity for the monoalkylated aromatic hydrocarbon was lower. In this gas-liquid-liquid reaction, the solubility of the reactants in the ionic phase (e.g. the benzene/ethene ratio in the ionic phase) and the mixing of the phases were probably critical. This is an example in which the engineering aspects are of the utmost importance. [Pg.276]

O Donnell [9] has described the engineering aspects of these special flowsheets. [Pg.6]

This form of corrosion is not of great concern from the engineering aspect, as the service life can be estimated within reasonable accuracy. Uniform corrosion can be prevented or reduced by using the following methods singly or in combination ... [Pg.1269]

The ID function involves a great deal more than appearance design. The designer is often called on to create the very concept of the product. In doing so, they will consider the utility, cost, innovation and human engineering aspects of the proposed product that relates to its basic appeal to the end-user. [Pg.17]

Additionally, a personal objective was to provide the information contained within this book in such a way that it could be used regularly in the field rather than be relegated to a bookshelf with other works of occasional reference. As such, although this book is essentially concerned with applied chemistry, I found it necessary to devote several of the initial chapters to a discussion on some basic but practical engineering aspects. Subjects covered include fluid dynamics, thermodynamics, the various types and designs of boilers to be found, and the function of all the critical system auxiliaries and components. The subject of boiler water chemistry is so inextricably bound up with the mechanical operation of boiler plants and all their various systems and subsystems that it is impossible to discuss one topic without the other. [Pg.1000]

TABLE 4.2 Chemical Engineering Aspects of Electronic, Photonic, and Recording Materials and Devices... [Pg.52]

Rubio-Hernandez F.J., Gomez-Merino A.I., Ruiz-Reina E., Carnero-Ruiz C. The primary electroviscous effect of polystyrene latexes. Colloids and Surfaces A Physicochemical and Engineering Aspects 140 (1998) 295-298. [Pg.115]

Concurrent with these investigations, polyphosphazene matrices, functionalized with aminoacid esters or with imidazole groups, became of importance because of their tissue engineering aspects in bone regeneration [655,656,679], treatment of periodontal diseases [657], and nerve reconstruction problems [680-682] in which the remarkable bio compatibility of POP matrices was coupled with their tuneable bio degradability. [Pg.217]


See other pages where Engineering aspects is mentioned: [Pg.438]    [Pg.438]    [Pg.438]    [Pg.438]    [Pg.438]    [Pg.438]    [Pg.438]    [Pg.438]    [Pg.265]    [Pg.1808]    [Pg.2143]    [Pg.1]    [Pg.2]    [Pg.52]    [Pg.519]    [Pg.773]    [Pg.774]    [Pg.748]    [Pg.613]    [Pg.615]    [Pg.149]    [Pg.502]    [Pg.57]   
See also in sourсe #XX -- [ Pg.35 ]

See also in sourсe #XX -- [ Pg.579 ]




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