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S flux

Although the global S cycle has been studied by several investigators (e.g., Holser and Kaplan, 1966 Holland, 1978), hydrothermal S flux has not been considered. Thus, hydrothermal S flux is estimated below. H2S concentration in midoceanic ridge hydrothermal solution is mo.stly in a range of (1-6) mmol/kg H2O (Gamo, 1995). [Pg.420]

Using this concentration and rate of seawater cycling (= (1 -4) x 1kg/m.y.), we obtain hydrothermal S flux from midoceanic ridge as (2-24) x lO mol/m.y. The most likely flux is 6 2 x lO mol/m.y. This estimated value is consistent with the value by Elderfield and Schultz (1996) which is (0.85-9.6) x lO mol/m.y. [Pg.420]

Shikazono and Kashiwagi (1999) estimated (4-22) x 10 kg/m.y. (mostly (6dz 2) x 10 kg/m.y.) as a rate of seawater cycling at present-day back-arc basin. Using these [Pg.420]

Sulfur in the sediments and oceanic crust which is derived from seawater subducts to deeper parts. This subduction flux is estimated to be ca. 4 x lO mol/m.y. (Shikazono, 1997). Therefore, degassing S flux from back-arc and island arc ((2.3-8.2) x lO mol/m.y.) seems to be not different from the subduction flux, although uncertainty of estimated degassing and subduction flux is large. [Pg.421]

We speculate from the above argument that primordial sulfur degasses from midoceanic ridges even at present time as well as He, because subduction flux to mantle seems to be small. However, we need more detailed study on long-term S cycle including hydrothermal S flux to evaluate this speculation. [Pg.421]


When the eore s flux is eompletely emptied prior to the next cyele, it is referred to as the discontinuous-mode of operation. This is seen in the induetor eurrent and voltage waveforms in Figure 3-4. When the eore does not eompletely empty itself, a residual amount of energy remains in the eore. This is ealled the continuous mode of operation and ean be seen in Figure 3-5. The majority of boost-mode eonverters operate in the diseontinuous mode sinee there are some intrinsie instability problems when operating in the eontinuous mode. [Pg.25]

Formation of Borides 6.7.4. Crystal Growth of Borides 6.7.4.S. Flux Methods... [Pg.291]

A commonly held belief is that, for an enzyme reaction within a metabolic pathway, a large excess of catalytic capacity relative to a pathway s metabolic flux ensures that a given step is at or near thermodynamic equilibrium. Brooks recently treated the kinetic behavior of reaction schemes one might judge to be at equilibrium, and he showed that individual steps can remain far from equilibrium, even at a high ratio of an enzyme s flux to a pathway s steady-state flux. His calculations indicate that whether a reaction is near equilibrium depends on (a) the overall flux through the enzyme locus and (b) the kinetic parameters of the other enzymes in the pathway. S. P. Brooks (1996) Biochem. Cell Biol. 74, 411. [Pg.271]

Total S content cannot indicate whether increased carbon inputs to sediments cause increased diffusion of sulfate into sediments or restrict reoxidation and release of S from sediments, because the net effect is the same. In a survey of 14 lakes, Rudd et al. (80) did not observe a strong correlation between organic matter content per volume and net diffusive flux of sulfate. However, in English lakes the lowest C S ratios occur in the most productive lakes (24) whether this represents enhanced influx or retarded release is not clear. Among 11 Swiss lakes, ratios of C to S sedimentation rates are relatively constant and substantially below C S ratios in seston net S fluxes... [Pg.353]

The turnover time (x) of a reservoir is its mixing or refresh rate, and is the time it would take for the reservoir to completely empty if there were no further inputs. For soils, it is a measure of the first-order kinetics for decay (x = Ilk). At steady state, it is calculated as the inventory divided by the total inputs (or total outputs) to the reservoir. To calculate the turnover time for a soil C reservoir at steady state, we would divide the mass of SOM (C) by the total carbon fluxes (.S ) from the reservoir or x = C/S. Fluxes would include decomposition to C02 and leaching of dissolved organic. [Pg.231]

Figure 9.23. Oceanic cycles of strontium and sulfur. Sr fluxes are in units of 109 moles y 1 S fluxes are in units of 1012 moles y1. The imbalance for S suggests storage of S042" in seawater. Figure 9.23. Oceanic cycles of strontium and sulfur. Sr fluxes are in units of 109 moles y 1 S fluxes are in units of 1012 moles y1. The imbalance for S suggests storage of S042" in seawater.
Consider para-dichlorobenzene (DCB), which is used as a toilet disinfectant. The following data are available for DCB the molecular weight is 146 g/mol, the liquid vapor pressure is 1.3 Torr, and the saturated water solubility is 5.3 x 10-4 mol/L. In Lake Zurich, the measured concentration of DCB is lOng/L and the average wind speed is 2.3 m/s. What is this compound s flux into or out of Lake Zurich ... [Pg.145]

The enhancement of the T Tauri-phase ultraviolet flux over the present sun s fluxes is clearly very wavelength-dependent (see also Table 1). Thus use of this average T Tauri spectrum should represent a significant improvement to our wavelength-independent treatment used previously as input for the photochemical models (Canuto et al., 1982). [Pg.78]

Satyanarayana SV, Bhattacharya PK, and De S. Flux decline during ultrafiltration of kraft black liquor using different flow modules A comparative study. Sep. Pur. Techn. 2000 20 155-167. [Pg.1005]

Flux of component i, mol/m s Flux of solute, mol/m s Flux of solvent, mol/m s Kozeny-Carman constant Distribution constant of solute Membrane thickness, m Phenomenological coefficients... [Pg.254]

ISlHnm Static Bed Height, 1.25-l(gim s Flux S9 C inlet Temperature... [Pg.1405]

The first equation describes the rate of accumulation of product that results from the monomolecular breakdown of intermediate complex the second states that the difference between the rate of production of intermediate complex by the bimolecu-lar reaction of free enzyme and substrate, and the rate of removal of intermediate complex by the forward and reverse monomolecular reactions, must appear as a change in the concentration of the intermediate complex. These equations are also referred to as mass balance equations, or Kirchhoff s flux equations. [Pg.103]

In the Power-Law Formalism each rate law is represented as a product of power-law functions [e.g., Eqn. (28)]. The fundamental equations governing the behavior of the intact biochemical system are Kirchhoff s flux equations, which are obtained by combining the rate laws for synthesis and degradation of each molecular constituent. There are a number of general strategies for combining the individual rate laws to obtain Kirchhoff s flux equations (see below) the simplest of these strategies allows one to write a local representation as... [Pg.128]


See other pages where S flux is mentioned: [Pg.1835]    [Pg.324]    [Pg.235]    [Pg.420]    [Pg.420]    [Pg.421]    [Pg.289]    [Pg.170]    [Pg.733]    [Pg.733]    [Pg.138]    [Pg.363]    [Pg.14]    [Pg.316]    [Pg.65]    [Pg.464]    [Pg.202]    [Pg.15]    [Pg.187]    [Pg.134]    [Pg.249]    [Pg.3863]    [Pg.4657]    [Pg.118]    [Pg.224]    [Pg.910]    [Pg.911]    [Pg.84]    [Pg.740]    [Pg.217]    [Pg.452]   


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