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Ammonia concentration

Sketch the titration curve for 50.0 mL of 5.00 X 10 M Cd + with 0.010 M EDTA at a pH of 10, and in the presence of an ammonia concentration that is held constant throughout the titration at 0.010 M. This is the same titration for which we previously calculated the titration curve (Table 9.15 and figure 9.27). [Pg.320]

Iron, cobalt, and nickel catalyze this reaction. The rate depends on temperature and sodium concentration. At —33.5°C, 0.251 kg sodium is soluble in 1 kg ammonia. Concentrated solutions of sodium in ammonia separate into two Hquid phases when cooled below the consolute temperature of —41.6°C. The compositions of the phases depend on the temperature. At the peak of the conjugate solutions curve, the composition is 4.15 atom % sodium. The density decreases with increasing concentration of sodium. Thus, in the two-phase region the dilute bottom phase, low in sodium concentration, has a deep-blue color the light top phase, high in sodium concentration, has a metallic bronze appearance (9—13). [Pg.162]

Ammonia.. The most rehable results for ammonia are obtained from fresh samples. Storage of acidified samples at 4°C is the best way to minimi2e losses if prompt analysis is impossible. The sample acidity is neutrali2ed prior to analysis. Ammonia concentrations of 10 -0.5 M can be determined potentiometricaHy with the gas-sensing, ion-selective electrode. Volatile amines are the only known interferents. [Pg.232]

Because the solution is capable of absorbing one mole of carbon monoxide per mole of cuprous ion, it is desirable to maximize the copper content of the solution. The ammonia not only complexes with the cuprous ion to permit absorption but also increases the copper solubiUty and thereby permits an even greater carbon monoxide absorption capacity. The ammonia concentration is set by a balance between ammonia vapor pressure and solution acidity. Weak organic acids, eg, formic, acetic, and carbonic acid, are used because they are relatively noncorrosive and inexpensive. A typical formic acid... [Pg.54]

TABLE 26-19 Comparison of Measured and Calculated Ammonia Concentrations in Ammonia Spill Tests... [Pg.2320]

If necessary, dilute the sample to give an ammonia concentration of 1 mg L 1 and fill a 50 mL Nessler tube to the mark. Prepare a series of Nessler tubes containing the following volumes of standard ammonium chloride solution diluted to 50 mL 1.0,2.0,3.0,4.0,5.0, and 6.0 mL. The standards contain 0.01 mg NH3 for each mL of the standard solution. Add 1 mL of Nessler s reagent to each tube, allow to stand for 10 minutes, and compare the unknown with the standards in a Nessler stand (Section 17.4) or in a BDH Nesslerimeter. This will give an approximate figure which will enable another series of standards to be prepared and more accurate results to be obtained. [Pg.680]

In a packed column, operating at approximately atmospheric pressure and 295 K, a 10% ammonia-air mixture is scrubbed with water and the concentration of ammonia is reduced to 0.1%. If the whole of the resistance to mass transfer may be regarded as lying within a thin laminar film on the gas side of the gas-liquid interface, derive from first principles an expression for the rate of absorption at any position in the column. At some intermediate point where the ammonia concentration in the gas phase has been reduced to 5%. the partial pressure of ammonia in equilibrium with the aqueous solution is 660 N/nr and the transfer rate is ]0 3 kmol/m2s. What is the thickness of the hypothetical gas film if the diffusivity of ammonia in air is 0.24 cm2/s ... [Pg.853]

Figure 8.23. The solid and monotonically declining line to the right represents the equilibrium curve. The four curves represent lines with constant rates in the same plot. Since we want to operate at points where of maximum ammonia concentration, the optimal operation line is defined as the line running parallel to the equilibrium curve, passing through all the maxima. [Adapted from I. Dybkjaer, in Ammonia Catalysis and Manufacture (1995) Ed. A. Nielsen. Springer-Verlag, Berlin/Heidelberg, p. 199.]... Figure 8.23. The solid and monotonically declining line to the right represents the equilibrium curve. The four curves represent lines with constant rates in the same plot. Since we want to operate at points where of maximum ammonia concentration, the optimal operation line is defined as the line running parallel to the equilibrium curve, passing through all the maxima. [Adapted from I. Dybkjaer, in Ammonia Catalysis and Manufacture (1995) Ed. A. Nielsen. Springer-Verlag, Berlin/Heidelberg, p. 199.]...
Figure 8.25. Predicted volcano plots for ammonia synthesis, showing the turnover frequency versus the relative bonding strength of N atoms to the surface for ammonia concentrations of 5%, 20%, and 90%. The left-hand panel corresponds to conditions of... Figure 8.25. Predicted volcano plots for ammonia synthesis, showing the turnover frequency versus the relative bonding strength of N atoms to the surface for ammonia concentrations of 5%, 20%, and 90%. The left-hand panel corresponds to conditions of...
The equilibrium curve and the optimal operation line are again plotted in an ammonia concentration versus temperature plot for each of the two sets of conditions in Fig. 8.26, but now together with the optimal catalyst curves for a few selected nitrogen bonding energies. The right-hand panel also shows the operating line, and it is now possible to estimate which catalyst should be where in the reactor. [Pg.334]

A complex was detected in these solutions with the composition CuCN but this was not formed in significant quantities under the conditions employed. The role of ammonia molecules could not be assessed, although it was found that the rate showed a strong inverse dependence in ammonia concentration, indicating competition between NHj and CN for coordination sites. [Pg.411]

The ammonium salts retard the depolytmerization, which is expressed by an increasing of the ammonia concentration and reducing of the ammonium hydroxide. The addition of Na and ions leads to enhancing of the process, but in this case the values are not so close as it is in the other processes. From the investigated divalent ions, we found out that Mg " retard the depolymerization, while Ca " enhance it. Comparing the influence of the ions on the performing reactions, we will notice that these which enhance the ammonolysis retard the depolymerization, and these which enhance the hydrolysis enhance the depolymerization as well. [Pg.533]

Xylose-rich pectic polysaccharide was extracted from defatted and protein-free cell wall preparation (5) using HCl solution (pH 1.6) at 85° C for 4 h. The extract was adjusted to pH 5.0 with ammonia, concentrated on a rotary evaporator under reduced pressure at 40°C, and precipitated with 5 volumes of 96% ethanol. After washing twice with 80% ethanol and drying in an air circulated oven at 40°C for 2 h, the pellet was ledissolved with distilled water and then precipitated with 4 vols 96% ethanol. Before the pellet was gently ground, the precipitated pellet was washed twice with 70% ethanol and dried at 40 ° in an air circulated oven for 16 h. The resultant white powder was labelled "xylose-rich pectic polysaccharide" and stored in a refrigerator. [Pg.638]

There is tentative evidence for the lower reactivity of the hexaammine species in high ammonia concentration. The tetraammine (diaquated) and lower ammine Co(II) species do not pick up O2 over relatively long periods (75). [Pg.10]

Ammonia (NH3) is just one of the toxins implicated in HE. It is a metabolic by-product of protein catabolism and is also generated by bacteria in the GI tract. In a normally functioning liver, hepatocytes take up ammonia and degrade it to form urea, which is then renally excreted. In patients with cirrhosis, the conversion of ammonia to urea is retarded and ammonia accumulates, resulting in encephalopathy. This decrease in urea formation is manifest on laboratory assessment as decreased blood urea nitrogen (BUN), but BUN levels do not correlate with degree of HE. Patients with HE commonly have elevated serum ammonia concentrations, but the levels do not correlate well with the degree of central nervous system impairment.20... [Pg.327]

Increased blood ammonia concentration is characteristic of hepatic encephalopathy, but levels do not correlate well with the degree of impairment. [Pg.328]

Draw up a preliminary flow-sheet for the manufacture of 20,000 t/y nitric acid (basis 100 per cent HNO3) from anhydrous ammonia, concentration of acid required 50 to 60 per cent. [Pg.150]

Excess air is supplied to the oxidiser to keep the ammonia concentration below the explosive limit (see Chapter 9), reported to be 12 to 13 per cent (Chilton), and to provide oxygen for the oxidation of NO to NO2. [Pg.152]

Guerrero, L., Omil, F., Mendez, R., and Lema, J.M., Treatment of saline wastewaters from fish meal factories in an anaerobic filter under extreme ammonia concentrations, Biores. Technol., 61, 69-78, 1997. [Pg.778]

Acetone Acetylene Alkali and alkaline earth metals, e.g. sodium, potassium, lithium, magnesium, calcium, powdered aluminium Anhydrous ammonia Concentrated nitric and sulphuric acid mixtures Chlorine, bromine, copper, silver, flourine or mercury Carbon dioxide, carbon tetrachloride, or other chlorinated hydrocarbons. (Also prohibit, water, foam and dry chemical on fires involving these metals - dry sand should be available.) Mercury, chlorine, calcium hypochlorite, iodine, bromine or hydrogen fluoride... [Pg.165]

The manifold design allows for the determination of ammonia concentration in the range 0.2-20 xg/l as NH4 over a salinity range 35- 10%o, with negligible interference from amino acids. [Pg.132]

To overcome the suppression effect of amines in the determination of ammonia, Hampson [56] investigated the effect of nitrite ions added either as nitrite or as nitrous acid. Figure 5.2 indicates that very considerable suppression by nitrite does occur, although it is not as strong as with any of the amines. Again, it is not great so long as the nitrite N concentration is less than the ammonia N concentration, but rapidly increases as the nitrite concentration exceeds the ammonia concentration. In fact, the nitrite modified method was found to be satisfactory in open seawater samples and polluted estuary waters. [Pg.133]

Fig. 4 Redundance analysis (RDA) on phytoplankton communities collected during the surveys of 2005-2006 and their relationship with the environmental variables, such as the Total Phosphorus (PTOT), Water Flow (WATFL), Total Suspended Solids (TSS), ammonia concentration (NH4), nitrate concentration (N03), and conductivity (COND). Acronyms were also used for phytoplankton taxa representation... Fig. 4 Redundance analysis (RDA) on phytoplankton communities collected during the surveys of 2005-2006 and their relationship with the environmental variables, such as the Total Phosphorus (PTOT), Water Flow (WATFL), Total Suspended Solids (TSS), ammonia concentration (NH4), nitrate concentration (N03), and conductivity (COND). Acronyms were also used for phytoplankton taxa representation...

See other pages where Ammonia concentration is mentioned: [Pg.20]    [Pg.42]    [Pg.340]    [Pg.340]    [Pg.350]    [Pg.273]    [Pg.2075]    [Pg.120]    [Pg.134]    [Pg.466]    [Pg.479]    [Pg.480]    [Pg.324]    [Pg.455]    [Pg.127]    [Pg.127]    [Pg.264]    [Pg.297]    [Pg.297]    [Pg.331]    [Pg.332]    [Pg.334]    [Pg.115]    [Pg.489]    [Pg.769]    [Pg.272]    [Pg.275]    [Pg.131]   
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