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Electrode profitability

The market for tar-based road binders has declined considerably for a variety of reasons. Less cmde tar is available and the profits from the sales of electrode pitch and wood-preservation creosote or creosote as carbon-black feedstock are higher than those from road tar. In most industrial countries, road constmction in more recent years has been concentrated on high speed motorways. Concrete, petroleum bitumen, or lake asphalt are used in the constmction of these motorways. In the United Kingdom, for example, the use of tar products in road making and maintenance had fallen from 330,000 t in 1960 to 100,000 t in 1975 and is less than 100 t in 1994, mainly based on low temperature pitch which is not suitable for electrode or briquetting binders, but which is perfectly satisfactory as the basis for road binders. [Pg.349]

For a profitable electrochemical process some general factors for success might be Hsted as high product yield and selectivity current efficiency >50%, electrolysis energy <8 kWh/kg product electrode, and membrane ia divided cells, lifetime >1000 hours simple recycle of electrolyte having >10% concentration of product simple isolation of end product and the product should be a key material and/or the company should be comfortable with the electroorganic method. [Pg.86]

The wide applicability of the electrochemical processes in the chemical processing industry (CPI) derives from the fact that the electron is a versatile reagent. Thus the electron can - unlike standard chemical reagents - be readily removed (oxidation) or added (reduction). Depending on its potential, the electrode can either oxidize or reduce various chemical species to convert them into profitably salable products without the undesirable byproducts. [Pg.124]

In a number of instances, it has been found not only possible but profitable to utilize electrical energy in the preparation of chemical materials, both in the laboratory and in the industries. For success in such work, careful attention must be paid to many details such as accurate control of intensity of current, current density at the electrodes, and the concentration of the electrolyte and there must be available a suitable source of current (three or four storage cells), ammeter, voltmeter, and a variable resistance—best, a slide rheostat. It is usually possible to construct the working cells from ordinary... [Pg.52]

Therefore, a hybrid cell has been designed in lmol L 1 LiPF6 in 1 1 ethylene carbonate/ diethyl carbonate electrolyte by combining graphite and activated carbon as negative and positive electrodes, respectively [113], The activated carbon electrode is stable in the potential window between 1.0 and 5.0 V vs. Li, whereas the graphite electrode can be polarized down to low potential values. The mass of the electrodes should be balanced to fully take profit of the performance... [Pg.363]

If an electrode has an irregular surface, it is sometimes more profitable to detect absorbed radiation rather than transmitted or reflected radiation. Radiation absorption causes an increase in electrode temperature that can be detected directly with a thermocouple or thermistor (photother-mal spectroscopy61). [Pg.277]

Metal electrodes have been so extensively studied in the past that one may profitably ask the question How does a semiconductor electrode differ from a metal electrode Although there are many differences, the two essential distinctions are (1) the low and readily variable electron density and (2) the existence of an energy gap, i. e. of a region of unallowed electronic energies. The many other differences can be shown to arise from these two. For example, because of the low electron density, one has sizable penetration of the interfacial electric fields into the bulk of the electrode. With metals significant fields penetrate no more than an angstrom or so inside the electrode with typical semiconductors the fields may be sizable at depths in excess of 10,000 A. In consequence the distributions of charge and potential at a semiconductor electrode are almost of a different kind from those at a metal electrode. [Pg.206]

When spectroelectrochemistry is used as a tool in reaction kinetics, it is important to know accurately the rate of generation of reactive intermediates, that is, the accurate potential of the working electrode. This requirement becomes a particular problem when an OTE is the preferred electrode because of the ohmic drop in the electrode itself and the nonuniform current distributions often encountered. For the OTTLEs in particular, the accurate modeling of the diffusion in the cell also leads to rather complicated mathematical equations [346]. The most profitable way of operation is therefore to use a potential-step procedure where the potential is stepped to a value at which the heterogeneous electron transfer reaction proceeds at the diffusion-controlled rate. In transmission spectroscopy the absorbance, AB(t), of the initial electrode product B, in the absence of chemical follow-up reactions, is given by Eq. (99) [347,348], where b is the extinction coefficient of B. [Pg.163]

The development of suitable contacts for polymer solar cells has directly profited from the developments in light-emitting diodes, due to the injec-tion/extraction similarity. Due to its lower barrier for hole transfer between most conjugated polymers and PEDOT PSS as compared to ITO, this highly doped polymer electrode was applied at an early stage in solar cells as... [Pg.13]

Fig. 13 Effect of insertion of LiF layers of different thickness between the polymer-fullerene blend and the aluminum electrode. The current-voltage characteristics indicate a more effective charge carrier injection (a), and as can be seen also from b and c, the fill factor as well as the open circuit voltage profit from LiF. (Reprinted with permission from [91], 2002, American Institute of Physics)... Fig. 13 Effect of insertion of LiF layers of different thickness between the polymer-fullerene blend and the aluminum electrode. The current-voltage characteristics indicate a more effective charge carrier injection (a), and as can be seen also from b and c, the fill factor as well as the open circuit voltage profit from LiF. (Reprinted with permission from [91], 2002, American Institute of Physics)...
In the past, many candidate processes failed to yield the required return on investment because reactor designs at the allowable capital investment were not available. In spite of this, applications for electrosynthesis with the required profitability are growing as electrochemical engineering with a "systems" approach develops. To apply some of the newer chemical proposals it will be necessary to develop even more accurate mathematical design models and more innovative three-dimensional low-voltage-drop electrodes. [Pg.93]

For many years researchers concentrated on rechargeable batteries on the basis of PAc, PAni or PPy apart from the short-lived exception mentioned above, technological and commercial factors have prevented the success they hoped for. Technologically, because the performance that could be achieved was in most cases well below that of battery systems on the market, and commercially, because even the battery with the new technologically attractive Li-PPP composite electrode cannot (yet) be produced and marketed at a profit [26],... [Pg.508]


See other pages where Electrode profitability is mentioned: [Pg.105]    [Pg.105]    [Pg.368]    [Pg.369]    [Pg.37]    [Pg.3]    [Pg.249]    [Pg.161]    [Pg.160]    [Pg.222]    [Pg.677]    [Pg.334]    [Pg.344]    [Pg.358]    [Pg.366]    [Pg.16]    [Pg.3]    [Pg.2715]    [Pg.16]    [Pg.161]    [Pg.597]    [Pg.604]    [Pg.351]    [Pg.270]    [Pg.92]    [Pg.507]    [Pg.164]    [Pg.289]    [Pg.338]    [Pg.82]    [Pg.5]    [Pg.8]    [Pg.408]    [Pg.4938]    [Pg.4942]    [Pg.410]   
See also in sourсe #XX -- [ Pg.209 ]




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PROFIT

Profitability

Profiting

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