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Steady-state carbon concentration

The effect of excess air rate on the steady-state carbon concentration and temperature profiles is shown in Figure 3. As can be seen, the effect of excess air rate on the carbon concentration profiles is not profound. On the other hand, even though the steady-state bed temperature profiles are essentially flat, the temperature level is strongly influenced by the excess air rate. [Pg.100]

Figure 2. Effect of bubble size on the (-----) steady-state carbon concentration... Figure 2. Effect of bubble size on the (-----) steady-state carbon concentration...
It should be noted that a carbon concentration of 0.014 g/cm corresponds to 1% by weight in the present study, indicating that the steady-state carbon concentrations in all cases studied are far less than 1% by weight for the type A combustor. [Pg.106]

Figure 6. Effect of carbon feed rate on the (---------) steady-state carbon concentration and (---------------) bed temperature profiles in the type A combustor... Figure 6. Effect of carbon feed rate on the (---------) steady-state carbon concentration and (---------------) bed temperature profiles in the type A combustor...
It has been illustrated that the bubble size has strong influences on both the transient and steady-state carbon concentrations. The effects of the carbon feed rate, expressed as the carbon feed rate function on the steady-state carbon concentration and bed temperature profiles are negligible under the conditions... [Pg.111]

MeV, ,ean 0.049 MeV) with a half-life of 5715 30 and this is sufficiently long to enable a steady-state equilibrium concentration to be established in the biosphere. Plants and animals therefore contain 1.2 x 10 °% of their carbon as whilst they are living, and this leads to a /3-activity of 15.3 counts per min per gram... [Pg.276]

Auger electron spectroscopy (AES) is particularly suited for surface analysis (depth 0.5-1 nm). AES depth profile analysis was employed to determine the thickness and composition of surface reaction layers formed under test conditions in the Reichert wear apparatus in the presence of four different ZDDPs additives at different applied loads (Schumacher et al., 1980). Using elemental sensitivity factors the concentration of the four elements (S, P, O, C) was determined at three locations corresponding to a depth of 1.8, 4.3, and 17 nm. No significant correlation between wear behavior and carbon or oxygen content of the reaction layer was observed. A steady state sulfur concentration is reached after a very short friction path. Contrary to the behavior of sulfur, phosphorus concentration in the presence of ZDDPs increases steadily with friction path, and no plateau value is reached. [Pg.157]

Fig. 6.13 Steady-state (SS) concentration of hydroxyl radicals ( OH) in water as a function of dissolved organic carbon (DOC) caused by dissolved natural organic matter (DNOM) [redrawn from Hoigne (1998), p. 117, Figure 15]. Fig. 6.13 Steady-state (SS) concentration of hydroxyl radicals ( OH) in water as a function of dissolved organic carbon (DOC) caused by dissolved natural organic matter (DNOM) [redrawn from Hoigne (1998), p. 117, Figure 15].
Classic pharmaco-kinetic consideration gives a theoretical steady state plasma concentration equal to production (dosing rate) divided by clearance, i.e. between 0.017 and 0.100 nmol/L. The conventional HPLC-ECD and HPLC-MS/MS methods have sensitivity close to that level. Using up-concentrations and a HPLC-ECD system with a non-commercially available carbon column Bogdanov et al. [19] reported plasma values of 0.014 - 0.070 nmol/L (4- 21 pg/ml), i.e. in close agreement with the theoretical values. [Pg.36]

The absorption of lithium is rapid and complete within 6 to 8 hours. The absorption rate of slow-release capsules is slower and the total amount of lithium absorbed lower than with other dosage forms. Lithium is not protein bound. The elimination half-life for elderly patients (39 hours) is longer than that for adult patients (24 hours), which in turn is longer than that for adolescent patients (18 hours). The time to peak serum concentration for lithium carbonate is dependent on the dosage form (tablets, 1-3 hours extended tab, 4 hours slow release, 3 hours). Steady-state serum concentrations are reached in 4 days, with the desirable dose targeted to give a maintenance lithium ion plasma concentration range of 0.6 to 1.2 mEq/L, with a level... [Pg.873]

In Eq. (2) 6c is the surface coverage of carbon and Xb is the weight fraction of carbon in the segregation layer of Ni (g carbon/g Ni). The concentration of carbon dissolved in Ni at the support side of the particle equals the saturation concentration of filamentous carbon in Ni during steady-state carbon filament growth (CNi,r= C>at) (7, 13). [Pg.96]

The situation is different when simulating the dynamics of the uptake of the carbon and energy source. Here, there is a high risk of failure if the dynamic behavior is predicted with Monod kinetics verified at different snapshot steady states in continuous or fed batch cultures. Application of these kinetics is questionable, because the steady state data of substrate uptake at different dilution rates may be corrupted by induction of different transporter systems depending on the steady state substrate concentrations. In addition to the variability of the affinity of the various transporter systems as clearly demonstrated for the yeast Saccharomyces cerevisiae, we do expect pronounced differences between permeases and phospho-transferase systems because of the clear distinctions in the influence of intracellular metabolites upon the uptake dynamics. [Pg.50]

This means that at the ignition point, the steady-state surface concentration of empty catalyst sites is double that of the equilibrium concentration. Before ignition, the steady-state concentration of adsorbed oxygen, x s, is very low. Therefore, the approximate surface concentration of adsorbed carbon monoxide in the vicinity of the ignition point is... [Pg.364]

The extent of reaction ( is determined by mass balancing the open system in steady state. The concentrations of carbon monoxide and carbon dioxide are measured by non-dispersive infrared spectroscopy (Binos, Rosemount), oxygen is determined by use of a magnetic device (Magnos 3, Hartmann fz Braun). [Pg.1113]

The results also indicated that even the steady-state carbon-conditioned LCS reactor was more active than the 304 reference reactor. Figure 5 shows the higher hydrogen and methane concentrations obtained in the LCS reactor as compared to the reference reactor. Carbon yield was much higher in low carbon steel than in the reference reactor, while ethylene yield was slightly lower than that in the reference reactor. Conversions (reaction rates) in low carbon steel were always 25-35% higher than those obtained in the reference reactor. [Pg.228]

Guests are visiting, and the plastic-sealed bedroom is to be used as a guest room. However, the room is now too cold because the heating ducts have been sealed off with plastic, so a small kerosene heater is put in the room. This heater uses 200 g/hr of fuel (assume it is C12H26), and is fairly clean-burning only 0.1% of the carbon atoms in the fuel are released as CO, the rest being burned to carbon dioxide. What is the steady-state CO concentration in the room with the heater turned on ... [Pg.448]

Catalytic activity on SO2 removal. Figure 4 illustrates effects of carbon deposition from benzene and pyridine on SO2 breakthrough profiles over pitch-based ACF at 30°C, in the presence of 10% H2O. The treatment by pyridine was very effective in decreasing the level of steady state SO2 concentration. The modified ACF showing 8% of carbon deposition from pyridine (Point 1) showed complete removal of SO2 for at least 15h at a W/F of 2.5x10 g min ml-i. However, the ACFs modified by benzene showed rather poor activities compared to the ACF modified by pyridine, even though the same increase of weight was obtained. [Pg.67]

Carbon Dioxide Transport. Measuring the permeation of carbon dioxide occurs far less often than measuring the permeation of oxygen or water. A variety of methods ate used however, the simplest method uses the Permatran-C instmment (Modem Controls, Inc.). In this method, air is circulated past a test film in a loop that includes an infrared detector. Carbon dioxide is appHed to the other side of the film. AH the carbon dioxide that permeates through the film is captured in the loop. As the experiment progresses, the carbon dioxide concentration increases. First, there is a transient period before the steady-state rate is achieved. The steady-state rate is achieved when the concentration of carbon dioxide increases at a constant rate. This rate is used to calculate the permeabiUty. Figure 18 shows how the diffusion coefficient can be deterrnined in this type of experiment. The time lag is substituted into equation 21. The solubiUty coefficient can be calculated with equation 2. [Pg.500]

This program helps calculate the rate of methanol formation in mol/m s at any specified temperature, and at different hydrogen, carbon monoxide and methanol concentrations. This simulates the working of a perfectly mixed CSTR specified at discharge condition, which is the same as these conditions are inside the reactor at steady-state operation. Corresponding feed compositions and volumetric rates can be calculated from simple material balances. [Pg.219]

The carbon-14 formed by this nuclear reaction is eventually incorporated into the carbon dioxide of the air. A steady-state concentration, amounting to about one atom of carbon-14 for every 1012 atoms of carbon-12, is established in atmospheric C02. More specifically, the concentration of C-14 is such that a sample containing one gram of carbon has an activity of 15.3 atoms/min. A living plant, taking in carbon dioxide, has this same activity, as do planteating animals or human beings. [Pg.519]

Once the model was complete, it was adjusted to a steady state condition and tested using historic carbon isotope data from the atmosphere, oceans and polar ice. Several important parameters were calculated and chosen at this stage. Sensitivity analysis indicated that results dispersal of the missing carbon - were significantly influenced by the size of the vegetation carbon pool, its assimilation rate, the concentration of preindustrial atmospheric carbon used, and the CO2 fertilization factor. The model was also sensitive to several factors related to fluxes between ocean reservoirs. [Pg.418]

The models also assume a steady-state condition which suggests that the carbon cycle is structured, stable, and balanced and will remain so indefinitely. This mechanistic view of biogeochemistry allows for little variation even though it is known that fluctuations and variation occur seasonally. The concentration of... [Pg.418]


See other pages where Steady-state carbon concentration is mentioned: [Pg.100]    [Pg.106]    [Pg.109]    [Pg.111]    [Pg.100]    [Pg.106]    [Pg.109]    [Pg.111]    [Pg.338]    [Pg.156]    [Pg.368]    [Pg.233]    [Pg.3127]    [Pg.152]    [Pg.194]    [Pg.344]    [Pg.718]    [Pg.210]    [Pg.194]    [Pg.235]    [Pg.54]    [Pg.323]    [Pg.96]    [Pg.132]    [Pg.54]    [Pg.6]    [Pg.384]    [Pg.30]    [Pg.6]    [Pg.78]    [Pg.423]   
See also in sourсe #XX -- [ Pg.106 , Pg.111 ]




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