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Processing additive

Moet et al. found by modeling the photocurrent that the use of 1,8-octanedithiol can prevent recombination-limited photocurrent in PCPDTBTPCeiBM solar cells [86]. Modeling showed that the decay rate of bound electron-hole pairs is reduced by additive addition resulting in dissociation probability of 70% at short-circuit current [Pg.20]

Morana et al. investigated the effect of ODT on the formation of the charge transfer complex (CTC) for C-PCPDTBT and Si-PCPDTBT [91]. Despite the pristine C-PCPDTBT, no changes were observed in the absorption spectrum of the Si-PCPDTBT films prepared with ODT. Enhanced phase segregation in the C-PCPDTBT films upon addition of ODT caused increase in the molecular luminescence to CT luminescence ratio. This is due to the reduced concentration of CT complexes by a decrease in the contact area between the polymer and the fullerene because of phase separation. [Pg.21]


Carbon, present in iron or remaining after inadequate degreasing, can form CO or CO2. Carbon particles may occur in the chlorate if graphite anodes were used in the production process. Additionally, barium peroxide contains carbonate as a contaminant. [Pg.485]

Papermaking additives can be categorized either as process additives or as functional additives. Process additives are materials that improve the operation of the paper machine, such as retention and drainage aids, biocides, dispersants, and defoamers they are primarily added at the wet end of the paper machine. Functional additives are materials that enhance or alter specific properties of the paper product, such as fillers (qv), sizing agents, dyes, optical brighteners, and wet- and dry-strength additives they may be added internally or to the surface of the sheet. [Pg.15]

Closed-Mill Concept. The closed-mill concept, or water circuit closure, has been studied by the pulp and paper industry for many years. In some parts of the paper manufacturing process, up to 98% of the water is recycled within the process, eg, the wet end of the paper machine. However, in the pulp mill, especiaUy kraft mills, effluents are produced owing to the need to purge from the system various metals that come in with the wood, as weU as organic by-products from the pulping process, additives, and especially chloride ions that originate in the bleach plant. [Pg.283]

Tobacco. Citric acid is a natural constituent of the tobacco leaf and during tobacco processing additional citric acid is added to enhance the flavor and to effect more complete combustion of tobaccos (212). [Pg.186]

In 1990 the majority of U.S. PCB production resulted from subtractive or print-and-etch processing additive processes were less than 6% of the total multilayer boards accounted for 55.8%. The ratio of rigid to flexible surface areas plated is about 15 1. High performance plastics including polyimide. Teflon, and modified epoxy comprised 6% of the market ( 324 million) flexible circuits were 6.6% ( 360 million) (42). [Pg.111]

The two fluids most often studied in supercritical fluid technology, carbon dioxide and water, are the two least expensive of all solvents. Carbon dioxide is nontoxic, nonflammable, and has a near-ambient critical temperature of 31.1°C. CO9 is an environmentally friendly substitute for organic solvents including chlorocarbons and chloroflu-orocarbons. Supercritical water (T = 374°C) is of interest as a substitute for organic solvents to minimize waste in extraction and reaction processes. Additionally, it is used for hydrothermal oxidation of hazardous organic wastes (also called supercritical water oxidation) and hydrothermal synthesis. [Pg.2000]

Larger steam turbine or bootstrap required Expander and generator part of process Addition of expander requires prior planning Induction M/G decreases power factor Loss of production on loss of generator or expander... [Pg.178]

Several constraints were faced in the design phase of the project. For example, special attention was given to the fact that 400 Series stainless steel, carbon, and some grades of aluminum were not compatible with the process. Additionally, the expander discharge temperature was required to stay between 35-70°F. The operating rpm of the expander wheel was determined by the rpm required by the third stage of the air compressor. [Pg.456]

Coal-tar pitch is particularly valuable to anode and electrode manufacturers The mam function is to plasticize coke gnst so that formed bodies can be extmded or molded without distortion during the later stages of processing Additionally, the pitch should give a high-carbon yield and not adversely affect the overall properties of the finished article. Although coal-tar pitch remains the bmder of choice, petroleum-based binders can perform satisfactorily for the aluminum industry [18]. [Pg.209]

The cyanohydrin of methyl perfluoroheptyl ketone was synthesized by a two-step process addition of sodium bisulfite and subsequent treatment with sodium cyanide. When the ketone was reacted with sodium cyanide, cyclic addition products were obtained, instead of the product of cyanohydrin formation. This result was attributed to the solubility characteristic of a long perfluoroalkyl group, which makes the compound less soluble in water and polar organic solvents [54] (equation 40) (Table 14). [Pg.638]

Zincke-type salts derived from other aromatic nitrogen heterocycles also undergo Zincke reactions. The isoquinolinium salt 6 (Scheme 8.4.16) permitted incorporation of a phenyl ethylamine chiral auxiliary, providing salt 48. In this context and others (vide infra), Marazano and co-workers found that refluxing -butanol was a superior solvent system for the Zincke process. Additionally, the stereochemical integrity of the or-chiral amino fragment was reliably maintained. [Pg.362]

Another approach used to reduce the harmful effects of heavy metals in petroleum residues is metal passivation. In this process an oil-soluble treating agent containing antimony is used that deposits on the catalyst surface in competition with contaminant metals, thus reducing the catalytic activity of these metals in promoting coke and gas formation. Metal passivation is especially important in fluid catalytic cracking (FCC) processes. Additives that improve FCC processes were found to increase catalyst life and improve the yield and quality of products. ... [Pg.47]

As you might have already gathered, the majority of industrial fermentations are batch processes. In closed batch systems, the growth medium is inoculated with cells and growth and product formation is allowed to proceed until the required amount of conversion has taken place. After harvesting the culture the vessel is cleaned, sterilised and filled with fresh medium prior to inoculation. For some processes, addition of all the feedstock prior to inoculation, as is done in closed batch fermentations, is undesirable and it is preferable to incrementally add the carbon source as the fermentation proceeds. Such a process is known as fed-batch culture and the approach is often used to extend the lifetime of batch cultures and thus product yields fed-batch cultures are considered further in Section 2.7.4. [Pg.19]

The really great advantage of the continuous methods over the batch methods is the much smaller accumulation of NG in any given plant location in the former process. Additional advantages accrue from faster production, better control, lower labor costs, etc. Klassen and Humphrys (Ref 40) compare the Biazzi con-... [Pg.239]

These novel organic polymers were not developed solely for the CW or BW treatment market but are for much wider application. These same value-adding process additives are regularly incorporated into products for industrial and domestic cleaning, concrete, pulp and paper, metal finishing, paints and surface coatings, wastewater, seawater distillation, drilling muds, secondary oil-recovery, plastics extrusion, fibers, rubbers, and a host of other areas. [Pg.439]

Great Lakes Chemical Corporation. Products for Industrial Water Treatment. Various technical/promotional literature. (Formerly FMC Corporation [UK] Ltd. and prior to that the Process Additives Division of Ciba-Geigy), UK, 1983-1995. [Pg.766]

Polyester chemistry is the same as studied by Carothers long ago, but polyester synthesis is still a very active field. New polymers have been very recently or will be soon commercially introduced PTT for fiber applications poly(ethylene naph-thalate) (PEN) for packaging and fiber applications and poly(lactic acid) (PLA), a biopolymer synthesized from renewable resources (corn syrup) introduced by Dow-Cargill for large-scale applications in textile industry and solid-state molding resins. Polyesters with unusual hyperbranched architecture also recently appeared and are claimed to find applications as crosstinkers, surfactants, or processing additives. [Pg.20]

Paraffinic oils are the least efficient as processing additives but the resulting vulcanizates have good aging and color retention properties and give the best low temperature performance. [Pg.1031]

Accordingly, serious commercially oriented attempts are currently being made to develop special gas-phase micro and mini reactors for reformer technology [91, 247-259], This is a complex task since the reaction step itself, hydrogen formation, covers several individual processes. Additionally, heat exchangers are required to optimize the energy balance and the use of liquid reactants demands micro evaporators [254, 260, 261], Moreover, further systems are required to reduce the CO content to a level that is no longer poisonous for a fuel cell. Overall, three to six micro-reactor components are typically needed to construct a complete, ready-to-use micro-reformer system. [Pg.97]

As shown in the reaction Scheme (6.16), the reaction that yields the poisoning intermediate is a chemical reaction, and no electrons are implied in the process. Additionally, the reaction takes place at open circuit, i.e., without potential control. This property has been used to measure the total amount of poisoning intermediate that can be accumulated on the surface. The amount and fraction of the surface blocked... [Pg.180]

Dynamar Polymer Processing Additive Technical Information, Parr Bomb Analytical Method for Determining Total Organic Fluorine Concentration in Polyethylene, Dyneon, Oakdale, MN (n.d.). [Pg.680]

Figure 3 Effect of seeding and inhibitors on aggregation reaction. The lag phase (curve c) is characteristic of reactions in which formation of nuclei for polymerization is an unfavorable process. Addition of preformed nuclei or seeds" (curve a) abolishes the lag phase. Inhibitors may affect the formation of nuclei and influence eitherthe lag phase, the extension of the nuclei changing the growth phase, or both (curve d). The inhibitor example (curve d) acts more strongly at nuclei formation than on the slope or plateau level of the growth phase. Figure 3 Effect of seeding and inhibitors on aggregation reaction. The lag phase (curve c) is characteristic of reactions in which formation of nuclei for polymerization is an unfavorable process. Addition of preformed nuclei or seeds" (curve a) abolishes the lag phase. Inhibitors may affect the formation of nuclei and influence eitherthe lag phase, the extension of the nuclei changing the growth phase, or both (curve d). The inhibitor example (curve d) acts more strongly at nuclei formation than on the slope or plateau level of the growth phase.
Wastewater treatment in the copper sulfate industry can further be improved, particularly the removal of the toxic metals, through sulfide precipitation, ion exchange, and xanthate processes. Addition of ferric chloride alongside alkaline precipitation can improve the removal of arsenic in the wastewater. [Pg.932]

In situ bioremediation In situ from soil and free product/ groundwater and treatment using aboveground processes Addition of oxygen or other... [Pg.1003]


See other pages where Processing additive is mentioned: [Pg.438]    [Pg.812]    [Pg.394]    [Pg.328]    [Pg.222]    [Pg.156]    [Pg.231]    [Pg.25]    [Pg.285]    [Pg.1069]    [Pg.358]    [Pg.1119]    [Pg.392]    [Pg.195]    [Pg.67]    [Pg.304]    [Pg.112]    [Pg.341]    [Pg.1044]    [Pg.109]    [Pg.495]    [Pg.1249]    [Pg.20]    [Pg.597]    [Pg.766]    [Pg.783]   


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