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Equilibrium mixing

According to Le Chatelier s principle the equilibrium will be shifted to the right-hand side by high pressures and, since the reaction is exothermic, by low temperatures. Indeed early work by Haber showed that at 200 °C and 300 atmospheres pressure the equilibrium mix would contain 90% ammonia, whilst at the same pressure but at 700 °C the percentage of ammonia at equilibrium would be less than 5%. Unfortunately the activation energy is such that temperatures well in excess of 1000 °C are needed to overcome this energy barrier (Figure 4.1). The conclusion from this is that direct reaction is not a commercially viable option. [Pg.84]

In general, r4 must be computed from a dynamic model for Hfle. /). However, for fully developed scalar fields (equilibrium mixing), the mixing time can be approximated from a model spectrum for ( c). [Pg.91]

Amine acid-base equilibrium mixing entropy... [Pg.93]

Adsorption of Two Surfactants. We now denote a quantity valid at the onset of micellization in the equilibrium mixed surfactant solution by the superscript c. Thus, the chemical potential of surfactant i in the mixed solution or in the mixed surface phase at the onset of micellization is given by... [Pg.229]

Reaction 3 provides a means for transferring an aryloxy unit from one radical to another. Hydrogen transfer reactions between phenols and aryloxy radicals occur so rapidly that the over-all reaction is a chain process which requires only initiation to proceed to the equilibrium mix-... [Pg.444]

The important point is, that the leads are actually in the equilibrium mixed state, the single electron states are populated with probabilities, given by the Fermi-Dirac distribution function. Taking into account all possible single-electron tunneling processes, we obtain the incoming tunneling rate... [Pg.236]

UOP/Toray Xylene, mixed C9 and C10 aromatics Toray TAC9 process produces equilibrium mixed xylenes from heavier aromatics 2 1997... [Pg.130]

In other words, the fewer axial hydroxyl groups the 1,6-anhydrohexo-pyranose contains, the more of it is present in the equilibrium mix-tureio2,io3 (see also, Ref. 104). The axial 3-hydroxyl group (or another... [Pg.35]

The breadth "of dispersion is measured by entropy, which ranges in value from zero for a pure state (idempotent density matrix) of a given energy, to a maximum for the stable equilibrium (thermodynamic equilibrium) mixed state of the same energy. [Pg.260]

Adenylic Acid. Adenosine 3 -monophosphate adenosine - 3 -phosphoric acid adenosine - 3 -monophos-phoric acid adenylic acid b yeast adenylic acid synadenylic acid h-adenylic acid. C HuNjOyP mol wt 347.23. C 34.59%, H 4.06%, N 20.17%, O 32.26%, P 8.92%. Early prepns from yeast nucleic acid Levene. Bass, Nucleic Acids, (Chemical Catalogue Co., New York, 1931). Early work probebty done on mixtures of 2 - and 3 -adenylic acids both compds isomerize readily to form an equilibrium mix -Hire under acid conditions Carter, Cohn, Fed. Proc. 8, 190 (1949) Baddily, in The Nucleic Acids vol. 1, E. Chargaff, J. N. Davidson, Eds. (Academic Press, New Yotk, 1955) pp 165-168 A. M. Michelson, The Chemistry of Nucleoside and Nucleotides (Academic Press, New York, 1963) pp 100-106. Synthesis Brnwn, Todd, J. Chem. Soc. 1952, 44. Structure nf dihydrate Brown el at, Nature 172, 1184... [Pg.26]

Application GT-lsomPX is GTC s xylene isomerization technology available in two versions ethylbenzene (EB) isomerization and EB dealkylation. Both versions gain high ethylbenzene conversion rates while producing equilibrium mixed xylenes—meta-xylene (MX), ortho-xylene (OX) and paraxylene (PX). [Pg.286]

A question that arises immediately, however, is that of the extent to which the solute component is also present atthe solid-vapor surface-i.e., the extent to which an equilibrium mixed adsorbed film is present. Qualitative observations by Bartell andFu tended to suggest that in their cases very little adsorption at the solid-vapor interface occurred, justifying their neglect of tt gyo. It would take the independent verification procedure suggested, however, to confirm the correctness of this assumption and of Equation 25. A complete study should include adsorption experiments with appropriate mixed vapors, so as to obtain tt g o independently. [Pg.67]

Styrene manufacture utilizes approximately 13 billion pounds of benzene each year. Existing technology alkylates benzene with ethylene and then dehydrogenates the ethylbenzene. Environmental considerations dictate that we should replace benzene, and the UCLA styrene process can. This process uses only mixed xylenes, which are more environmentally frieniy than benzene. The UCLA styrene process converts equilibrium mixed xylenes, the cheapest aromatic source available, to styrene in a single high-temperature step. The mechanism of this remarkable oxidative rearrangement is complex, but the overall process is very simple. [Pg.114]

The ease of formation of pseudobases (carbinolamines) from a variety of isoquinolinium salts has been investigated. Increasing pH facilitates pseudobase formation. Nitidine forms a pseudobase more readily than berberine, while 6,7-dimethoxy-2-methylisoquinoline did not form a pseudobase even at pH 13.2 Sanguinarine and chelerythrine acetates exist in an equilibrium mix-... [Pg.284]

With the development of the equation of state theories, however, phase diagrams began to be constructed. To everyone s surprise, virtually all these systems exhibited LCST behavior. (Earlier, many scientists were trying to raise the temperature to bring about miscibility.) It was discovered that for very small domains, equilibrium mixing could be achieved in a matter of minutes. The concept of specific interactions was developed, where hydrogen bonds,... [Pg.164]

Based on the assumption of equilibrium mixing in the feed grooves, increasing end flow from the feed grooves not only decreases the lubricant outlet temperature, but also significantly decreases the bearing film temperatures. [Pg.64]

In quantum information processing by NMR one of the major challenges is relaxation or decoherence. Often it is found that the equilibrium mixed state of... [Pg.242]

Remember that this form is motivated from a high temperature approximation for the NMR equilibrium density matrix, for which e = hcoL/2"kBT. But, whatever the situation, one must have Tr(l) = 2" and Tr(/0i) = 1. Consequently, Tr(/Oe) = 1, as it must be for density matrices. The matrix p can represent an equilibrium mixed state, or a pseudopure state. In particular, it can represent an entangled state. For instance, for two-qubits it could be the cat-state ... [Pg.207]

Based on mechanistic and kinetic studies of the higher alcohol synthesis from synthesis gas, it has been shown that the ethanol in the mixed-oxygenate product is produced from intermediates derived from methanol, not CO [103,109]. Kinetic models of the synthesis have been developed that are able to explain the observed product distribution [110,111]. These models are based on a detailed understanding of the reaction mechanism in which two types of reactions dominate aldol condensation, which yields primarily 2-methyl branched alcohols, and Cl coupling reactions, which yield linear alcohols [106,111]. Estimates of the parameters of the kinetic models that quantitatively describe the oxygenate product distributions suggest that the rate of ethanol formation is about an order of magnitude lower than the rate of production of branched alcohols [111,112]. On the Cs/Cu/Zn catalysts, this results in a minimum in yield of ethanol compared with the yields of methanol, 1-propanol, and 2-methyl-1 propanol. Althou methanol conversion to ethanol has been confirmed as part of the hi er alcohol synthesis from synthesis gas, this synthesis does not offer a plausible route for the conversion of methanol to ethanol. Under the reaction conditions methanol rapidly decomposes, even at a pressme of 0.1 MPa [113], to yield an equilibrium mix of methanol, CO, and H2. Furthermore, as shown by the data in T able 7, the yield of ethanol remains low even with methanol in the feed. [Pg.201]


See other pages where Equilibrium mixing is mentioned: [Pg.394]    [Pg.59]    [Pg.247]    [Pg.158]    [Pg.93]    [Pg.132]    [Pg.174]    [Pg.417]    [Pg.232]    [Pg.288]    [Pg.383]    [Pg.64]    [Pg.811]    [Pg.93]    [Pg.499]    [Pg.430]    [Pg.480]    [Pg.275]    [Pg.45]    [Pg.120]    [Pg.120]    [Pg.394]    [Pg.239]    [Pg.8451]    [Pg.66]    [Pg.4]   
See also in sourсe #XX -- [ Pg.153 ]




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Equilibrium Adsorption Properties of Single and Mixed Surfactant Solutions

Equilibrium constant, mixed micelle

Mixed equilibrium constant

Mixed equilibrium-dynamic modeling

Mixed oxides, phase equilibria

Mixed oxides, phase equilibria metal-oxygen

Mixed phase equilibria

Mixed solvent influence on the chemical equilibrium

Mixed solvent influence on the conformer equilibrium

Mixed-valence complexes comproportionation equilibrium

Mixing-segregation equilibrium

Phase equilibria and mixing reactions

Thermodynamic phase-equilibrium mixing process

Vapor-Liquid Equilibrium Modeling with Two-Parameter Cubic Equations of State and the van der Waals Mixing Rules

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