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Ammonium consumption rates

The ammonium flux from the anaerobic zone (where NFI4 is in high concentrations) to aerobic zone (where the concentration is low) is regulated by many factors ammonium concentration gradient, ammonium production rate, CEC, adsorption-desorption, intensity of soil reduction, temperature, bioturbation and mixing, and ammonium consumption rate. [Pg.322]

Equation 6.9 is based on the oxygen consumption rates measured over a period of 70 h. Phase 1 reflects chemical oxidation and is primarily regulated by the concentration of reduced inorganic species such as Fe(II). Neither A j nor A , was correlated with the total or water extractable carbon, which suggests that the oxygen consumption was dominated by reducible Fe(II) and ammonium (which are much more sensitive to oxygen than organic carbon). It is likely that some of the water-soluble Fe(II)... [Pg.209]

Ammonium flux from anaerobic soil layer is governed by the (1) concentration gradient established as a result of ammonium consumption in the aerobic zone due to nitrification and ammonia volatilization, (2) ammonium regeneration rate in the anaerobic soil layer, (3) adsorption coefficient for ammonium, (4) soil CEC, (5) intensity of soil reduction and accumulation of reduced cations, (6) bioturbation at the soil-floodwater interface, and (7) soil porosity. [Pg.318]

Figure 10.27 depicts both spectral efficiency and pointance in 2-3 pm band for the ammonium salt-based pyrolant, MAV, and the guanidinium based-salt pyrolant, MGV (with 10.5 wt% Viton each). The exothermal decomposition of the tetrazolate also influences the mass consumption rate, which drops with increasing Mg content This causes the pointance to decrease with increasing Mg content [45]. [Pg.177]

The single largest market for quaternary ammonium compounds is as fabric softeners. In 1993 this market accounted for over 50,000 metric tons of quaternaries in the United States (235). Consumption of these products is increasing at an annual rate of about 2—3%. The hair care market consumed over 9000 metric tons of quaternary ammonium compounds in 1992 (236). The annual consumption for organoclays is estimated at 12,700 metric tons (237). Esterquats have begun to gain market share in Western Europe and growth is expected to continue. [Pg.382]

The main advantages of the Cosorb process over the older copper ammonium salt process are low corrosion rate, abiHty to work in carbon dioxide atmospheres, and low energy consumption. The active CuAlCl C H CH complex is considerably more stable than the cuprous ammonium salt, and solvent toluene losses are much lower than the ammonia losses of the older process (94). [Pg.57]

To prevent accummulation of ammonium ions in consumption fish production ponds the water must be refreshed continously at a rather high rate. One process to remove the ammonium ions is the use of immobilized bacteria in porous particles with a particle size of 2 mm. Calculate the size of the plug flow reactor with a bed porosity of 0.5 by which 1 m of pond water can be treated per minute. [Pg.437]

Epoxides. Epoxy compounds react with the carboxyl groups of CTPB to form polyesters. The reaction rates and extent of reaction of a number of epoxides have been determined with the model compound hexanoic acid (6). It was found that most epoxides undergo side reactions (as evidenced by the more rapid consumption of epoxide species) but that at least one difunctional epoxide, DER-332 (Dow Chemical Co.) (Table IV), exhibits a clean reaction with carboxylic acids, even in the presence of ammonium perchlorate. [Pg.139]

The results of model compound studies with three different types of epoxides, obtained in the presence and absence of ammonium perchlorate are shown in Figures 4, 5, and 6. The epoxide DER-332 shows a uniform rate of disappearance for the acid and epoxide species in this reaction. In the presence of ammonium perchlorate, the rate is increased, and a minimum of side reactions occur. Similar data but faster reaction rates are obtained with Epon X-801, but the consumption of epoxide species by side reactions is increased, particularly in the presence of ammonium perchlorate. On the other hand, the epoxide ERLA-0510 (Table IV), which contains a basic nitrogen, shows a reaction rate which is an order of magnitude greater than that for DER-332, accompanied by a substantial increase in side reactions. In the presence of ammonium perchlorate, the side reactions of ERLA-0510 predominate. In all probability, the side reactions of the multifunctional epoxides studied are homopolymerization. [Pg.140]

Goddard, J. B. and Brosnahan, D. R. "Rate of Consumption of Dissolved Oxygen During Ammonium Carbonate In Situ Leaching of Uranium" Mining Engineering 1982 34 (11), 1589-1596. [Pg.293]

Typical kinetic profiles (hybridoma). (A) Cell concentration and viability (B) glucose consumption (GLC) and lactate production (LAC) (C) monoclonal antibody production (mAb) (D) glutamine consumption (GLN) and ammonium production (NH4+) (E) specific growth rate (px) (F) alanine (ALA) and glycine (GLY) production. Adapted from Lee (2003). Symbols correspond to the experimental data and the lines to the manual curve fitting. Vertical lines indicate the instant at which exponential growth phase ended (gx < Px.max)-... [Pg.184]


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Consumption rates

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