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Process Particularities

Besides the already mentioned criteria the design of the crystallisation processes is influenced by several additional factors. These are explained in the following sections. [Pg.205]


Many processes, particularly in the petrochemical industries, produce a reactor efiiuent which consists of a mixture of low-boiling components such as hydrogen and methane together with much less... [Pg.107]

Used in reprographic processes, particularly the ozalid blue-print paper processes. [Pg.133]

The properties required by jet engines are linked to the combustion process particular to aviation engines. They must have an excellent cold behavior down to -50°C, a chemical composition which results in a low radiation flame that avoids carbon deposition on the walls, a low level of contaminants such as sediment, water and gums, in order to avoid problems during the airport storage and handling phase. [Pg.178]

After passing through several stages of processing, gas pressure may need to be increased before it can be evacuated, used for gas lift or re-injected. Inter-stage pressure increases may also be required for further processing, particularly where wellhead pressure is low. Gas is compressed to increase its pressure. [Pg.252]

Processing heavy oils and bitumens represents a challenge for the current refinery processes, because heavy oils and bitumens poison the metal catalysts used m the refineries. In our research at the Loker Institute, we found the use of superacid catalysts, which are less sensitive to heavy oils, an attractive solution to their processing, particularly hydrocracking. [Pg.131]

Like methylolureas, cycHc ureas are based on reactions between urea and formaldehyde however, the amino resin is cycHc rather than linear. Many cychc urea resins have been used in textile-finishing processes, particularly to achieve wrinkle resistance and shrinkage control, but the ones described below are the most commercially important. They ate all in use today to greater or lesser extents, depending on specific end requirements (see also Textiles, finishing). [Pg.329]

Removal Processes. Pollutant removal processes, particularly dry deposition and scavenging by rain and clouds, are a primary factor in determining the dynamics and ultimate fate of pollutants in the atmosphere. [Pg.382]

The corrosion conditions can be different at the fluid line from the bulk condition. Aqueous liquids have a concave meniscus, which creates a thin film of liquid on the vessel wall immediately above the liquid line. Some corrosion processes, particularly the diffusion of dissolved gases, are more rapid in these conditions. Additionally, the concentration of dissolved gases is highest near the liquid surface, especially when agitation is poor. Locally high corrosion rates can therefore occur at the liquid line, leading to thinning in a line around the vessel. This effect is reduced if the liquid level in the vessel varies with time. Any corrosion tests undertaken as part of the materials selection procedure should take this effect into account. [Pg.902]

Alcohols with a C8 - Cn chain length, characterized by low solubility in aqueous media, may have a particular commercial potential as perspective extractants for tantalum and niobium hydrometallurgical processing. Particular emphasis has been placed recently on the investigation of tantalum and niobium extraction using octanol (C8Hi80) in the forms of 1-octanol and 2-octanol [462,466-473]. [Pg.280]

First, it is important to note that complete fluorination of the elements ensures an effective separation process. Particularly, Maiorov and Nikolaev [477] developed and reported on the conversion of tantalum, niobium and titanium sulfates and chlorides into their respective fluorides. It was shown that such conversion leads to significant improvement in/enhancement of the separation of the elements. [Pg.282]

The tendency to undergo valence isomerization is generally of fundamental importance regarding the stability of the compounds. In the case where an equilibrium exists between the eight-membered ring and the bicyclo[4.2.0]octatriene, decomposition may readily occur by a [2 + 2] cycloreversion process, particularly if molecular nitrogen or a cyano compound can be eliminated. [Pg.509]

Chronoamperometry is often used for measuring the diffusion coefficient of electroactive species or the surface area of the working electrode. Analytical applications of chronoamperometry (e.g., in-vivo bioanalysis) rely on pulsing of the potential of the working electrode repetitively at fixed tune intervals. Chronoamperometry can also be applied to the study of mechanisms of electrode processes. Particularly attractive for this task are reversal double-step chronoamperometric experiments (where the second step is used to probe the fate of a species generated in the first step). [Pg.61]

SOMe the enhancement in the meta-position is almost as large as in the para-position. The authors go on to show the applicability of op (g) values to certain solution processes, particularly those in non-aqueous solvents, but including the dissociation of thiophenols in 48% ethanol, the results of Bordwell and Andersen80 to which reference has been made earlier (Section III.A.1). A separation of field/inductive and resonance effects is also essayed for the gas-phase acidities of the phenols, and SOMe and S02Me feature in the discussion. There is reference to a oR° value of + 0.07 for SOMe as an unpublished result of Adcock, Bromilow and Taft (cf. 0.00 from Ehrenson and coworkers65 and — 0.07 from Katritzky, Topsom and colleagues128.)... [Pg.517]

Generally CVD is a captive operation and an integral part of a fabrication process, particularly in microelectronics where most manufacturers have their own CVD facilities. It is also an international business, and, while the U.S. is still in the lead, a great deal of work is under way, mostly in Japan and Europe. A significant trend is the internationalization of the CVD industry, with many multi-national ventures. [Pg.4]

The number of oxides is large since most metallic elements form stable compounds with oxygen, either as single or mixed oxides. However, the CVD of many of these materials has yet to be investigated and generally this area of CVD has lagged behind the CVD of other ceramic materials, such as metals, carbides, or nitrides. The CVD of oxides has been slower to develop than other thin-film processes, particularly in optical applications where evaporation. [Pg.295]

The mentoring relationship begins (the mentoring processes, particularly the first few meetings, have already been discussed in Chapter 6). As you will remember, one of the most important parts of the early stages of a relationship... [Pg.239]

Intensive technologies are derived from the processes used for the treatment of potable water. Chemical methods include chlorination, peracetic acid, ozonation. Ultra-violet irradiation is becoming a popular photo-biochemical process. Membrane filtration processes, particularly the combination microfiltration/ultrafiltra-tion are rapidly developing (Fig. 3). Membrane bioreactors, a relatively new technology, look very promising as they combine the oxidation of the organic matter with microbial decontamination. Each intensive technique is used alone or in combination with another intensive technique or an extensive one. Extensive... [Pg.100]

While our specific example is based upon control of batch polymerizations, the procedure we outline could, we feel, be applied equally well to selecting automation tools for many other kinds of processes, particularly those not truly well understood at the outset. [Pg.470]

The addition of metal hydrides to C—C or C—O multiple bonds is a fundamental step in the transition metal catalyzed reactions of many substrates. Both kinetic and thermodynamic effects are important in the success of these reactions, and the rhodium porphyrin chemistry has been important in understanding the thermochemical aspects of these processes, particularly in terms of bond energies. For example, for first-row elements. M—C bond energies arc typically in the range of 2, i-. i() kcal mol. M—H bond energies are usually 25-30 kcal mol. stronger, and as a result, addition of M—CH bonds to CO or simple hydrocarbons is thermodynamically unfavorable. [Pg.298]

Many of these compounds—puromycin and cycloheximide in particular—are not cfinically useful but have been important in elucidating the role of protein synthesis in the regulation of metabolic processes, particularly enzyme induction by hormones. [Pg.372]


See other pages where Process Particularities is mentioned: [Pg.269]    [Pg.8]    [Pg.437]    [Pg.88]    [Pg.262]    [Pg.516]    [Pg.86]    [Pg.90]    [Pg.440]    [Pg.374]    [Pg.480]    [Pg.462]    [Pg.30]    [Pg.276]    [Pg.728]    [Pg.654]    [Pg.7]    [Pg.1031]    [Pg.414]    [Pg.317]    [Pg.222]    [Pg.338]    [Pg.168]    [Pg.203]    [Pg.262]    [Pg.51]    [Pg.409]    [Pg.232]    [Pg.240]    [Pg.165]    [Pg.328]   


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