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Sizing reactions

Condensation of metal vapors followed by deposition on cooler surfaces yields metal powders as does decomposition of metal hydrides. Vacuum treatment of metal hydrides gives powders of fine particle size. Reaction of a metal haHde and molten magnesium, known as the KroU process, is used for titanium and zirconium. This results in a sponge-like product. [Pg.182]

Storage vessels can be made in a large variety of shapes and sizes. Absorption and distillation towers are available in several different forms and many sizes. Reaction vessels such as coppers, stills and Cellarius receivers can be supplied in the special materials to withstand thermal shock. Valves and pumps of many types are available to suit all conditions. Piping can be... [Pg.911]

Figure 15. Turnover rate for cyclohexene hydrogenation and dehydrogenation as a function of particle size. Reaction conditions are lOTorr CeHio, 200 Torr H2, and 310K for hydrogenation and 448 K for dehydrogenation, respectively [18]. Figure 15. Turnover rate for cyclohexene hydrogenation and dehydrogenation as a function of particle size. Reaction conditions are lOTorr CeHio, 200 Torr H2, and 310K for hydrogenation and 448 K for dehydrogenation, respectively [18].
Entry Batch size Reaction temp., time Process time Isol. yield Purity Remarks... [Pg.139]

Effect of geminal vs. vicinal substitution on EM s for ring-closure reactions Ring size Reaction and relative EM... [Pg.214]

Pentafluoroethane, catalytic synthesis, 39 344 Pentane, 37 170-171, 173, 197 catalyst particle size, reaction mechanisms and, 30 72-85... [Pg.172]

If the reaction is slow compared to diffusion so that the diffuso-reactive length is about the same or larger than the particle size, reaction takes place throughout the entire volume of the particle. On the other hand, if reaction is very fast compared to diffusion, i.e., the diffuso-reactive length is small compared to the size of the particle, reaction occurs close to the interface in this case, it is the surface area, rather than the volume, that determines the magnitude of the reactive uptake (e.g., see Fried et al, 1994). [Pg.163]

The hydrodynamic repulsion of two spheres is largest when both spheres are of equal size and thereby both particles prevent the escape of the intervening solvent equally. If one or other particle is much smaller than the other, then the hydrodynamic length is determined by the smaller particle s size. Reaction between a macromolecule and a molecular species would not display much evidence for hydrodynamic repulsion. [Pg.269]

Figure 1. Postulated sizing reactions of (a) alkyl ketene dimers and (b) alkyl succinic anhydrides. R. and R are short alkyl chains. Cell-OH represents cellulose. Figure 1. Postulated sizing reactions of (a) alkyl ketene dimers and (b) alkyl succinic anhydrides. R. and R are short alkyl chains. Cell-OH represents cellulose.
Chemical reactors are the most important features of a chemical process. A reactor is a piece of equipment in which the feedstock is converted to the desired product. Various factors are considered in selecting chemical reactors for specific tasks. In addition to economic costs, the chemical engineer is required to choose the right reactor that will give the highest yields and purity, minimize pollution, and maximize profit. Generally, reactors are chosen that will meet the requirements imposed by the reaction mechanisms, rate expressions, and the required production capacity. Other pertinent parameters that must be determined to choose the correct type of reactor are reaction heat, reaction rate constant, heat transfer coefficient, and reactor size. Reaction conditions must also be determined including temperature of the heat transfer medium, temperature of the inlet reaction mixture, inlet composition, and instantaneous temperature of the reaction mixture. [Pg.218]

Moreover, the inner cavity of supramolecular capsules provides a discrete, well-defined environment ideally suited to investigate effects of compartmentalization and processes in confined spaces [8]. To realize technical applications as detection and stabilization of encapsulated molecules or their use as nano-sized reaction vessels, precise control of important factors such as size, stability, porosity of the walls, and functionalization of the inner surface have to be achieved [9-18]. Several capsules have been synthesized and a proof of principle for several applications has been provided, but in most cases their use is restricted to small guest molecules. The development of spacious architectures which are able to encapsulate several bulky molecules and are amenable for decoration of the inner surface with functional groups will constitute an important step on the way to functional systems. [Pg.100]

Digestion. The influence of ultrasound on the dissolution kinetics of phosphate rock in HNO3 solutions [11] and variables affecting it (viz. particle size, reaction temperature, acid concentration, amplitude of US power) were studied by Tekin [12]. The term dissolution in the presence of auxiliary energy and an acid seems inappropriate in this case as the process is more like a true digestion. Another case in point is the dissolution of pyrite ores in acid and Fe2(S04)3 solutions, which is improved by 30% with respect to the absence of US energy [13]. [Pg.42]

Several options are available for nonroutine synthesis, such as heating and cooling the reaction vessel as well as feedback control using additional monitoring equipment. It is also possible to order custom sized reaction vessels, an optional mechanical stirrer, and a 200-L waste container. [Pg.831]

In 1989, Advanced ChemTech (ACT) introduced the Model 350 Simultaneous Multiple Peptide Synthesizer capable of assembling up to 96 peptides at scales from 5 to 50 pmol using the Fmoc method. Two different sized reaction vessels are available 600 pL and 1.5 mL. The first Model 350 was originally designed similar to the SMPS 350 by Zinsser, however during the next several years, ACT added additional features, such as an orbital shaker for resin agitation to differentiate the product. ... [Pg.835]

The kinetic studies make use of the unequally sized reaction partners (e.g. a large electron donor and a small electron acceptor couple) and benefit from the low viscosity of dichloromethane (DCM), both of which elevate the diffusion-controlled limit. To study the electron transfer, deoxygenated DCM solutions of, for example, w-terphenyl at high concentrations (0.02 m) were irradiated in the presence of different concentrations of fullerene (ca 10 m) [62]. This resulted in accelerated decay of (arene) + UV-Vis absorption, with rates linearly depending on fullerene concentration [62]. Formation of the electron-transfer product, fullerene", was confirmed spectroscopically by measurement of the NIR fingerprint (Amax = 1080 nm) [62, 65]. [Pg.939]

Due to the small volumes and feature sizes, reaction rates are found to be quite different in the microbiosensor system in comparison to their macro counter part. Most of this is due to the fact that diffusion is not the limiting factor in a reaction any longer. For example, the diffusion time of a particle with a diffusion coefficient = 10 m s is 15 min to travel a distance of 1 mm, but only 10 s to travel 100 /rm and only 0.1 s to travel 10/rm [37]. Therefore, DNA hybridization reactions, antibody-antigen binding events, and enzyme—substrate catalytic reactions take place in a fraction of the time required earlier. DNA hybridization can be accomplished in a matter of seconds in a microchannel system, while it takes in the order of an hour when employing standard Northern or Southern Blotting techniques with a piece of nylon membrane soaking in several milliliters of hybridization solution. [Pg.472]

A composite biomaterial formed by Pd metal, carbon-ceramic mixture and oxidoreductase enz3ones constitutes a new t3rpe of renewable smface biosensor with a controllable size reaction layer [198]. The carbon provides the electrical conductivity, the enzymes are used for biocatalyst process, metallic palladimn is used for electrocatalysis of biochemical reaction product and the porous silica provides a rigid skeleton. The hydrophobicity of this composite material allows only a limited section of the electrode to be wetted by the aqueous analyte, thus providing a controlled thickness reactive layer. Another biocomposite material containing enzyme-modifled boron-doped diamond was used in the development of biosensors for the determination of phenol derivatives [199], alcohol [200] and glucose [201]. [Pg.518]

Beyond the ability to investigate how reactions vary with increasing cluster size, reactions of vdW molecules can be used for doing selective chemistry. By... [Pg.207]


See other pages where Sizing reactions is mentioned: [Pg.2421]    [Pg.218]    [Pg.30]    [Pg.116]    [Pg.164]    [Pg.133]    [Pg.87]    [Pg.356]    [Pg.170]    [Pg.94]    [Pg.6]    [Pg.49]    [Pg.432]    [Pg.225]    [Pg.142]    [Pg.36]    [Pg.34]    [Pg.43]    [Pg.290]    [Pg.117]    [Pg.396]    [Pg.382]    [Pg.4]    [Pg.13]    [Pg.31]    [Pg.106]    [Pg.37]    [Pg.172]   
See also in sourсe #XX -- [ Pg.6 , Pg.7 , Pg.8 ]




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Aldol reaction ring size

Bromination Reaction on Resin Beads of Various Sizes

Claisen reaction ring size

Correlation between Metal Particle Size and Reaction Mechanisms

Cyclization reactions ring size effect

Dieckmann reaction ring size

Friedel-Crafts reaction ring size

Hydrogen addition reactions with cluster size-dependent

Metallo-ene reactions ring size

Microdroplet size effect on mass transfer and reaction rate

Oxygen reduction reaction catalyst size effect

Paper size reaction

Pellet size reaction rate, effect

Reaction parameters catalyst particle size

Reaction rate catalyst particle size effect

Ring size effect, catalytic reactions

Runaway reactions relief vent sizing

Shape selective reactions pore size effect

Sizing methods for bottom relief (dumping) of gassy reactions

Solid-state reactions particle size

The Relationship Between Activation or Reaction Volume and Ring Size

Two-Phase Flow Relief Sizing for Runaway Reaction

Type size chemical reactions

Worked example of relief system sizing for a tempered hybrid runaway reaction

Worked example of.Relief system sizing for a gassy runaway reaction

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