Modified nomogram for derivation of renal threshold phosphate concentration

2017 ◽  
Vol 49 (7) ◽  
pp. 1309-1310
Author(s):  
Mustafa Tosur
1982 ◽  
Vol 57 (3) ◽  
pp. 217-223 ◽  
Author(s):  
K Kruse ◽  
U Kracht ◽  
G Gopfert

The Lancet ◽  
1975 ◽  
Vol 306 (7929) ◽  
pp. 309-310 ◽  
Author(s):  
R.J. Walton ◽  
O.L.M. Bijvoet

2000 ◽  
Vol 42 (3-4) ◽  
pp. 265-272 ◽  
Author(s):  
T. Inoue ◽  
Y. Nakamura ◽  
Y. Adachi

A dynamic model, which predicts non-steady variations in the sediment oxygen demand (SOD) and phosphate release rate, has been designed. This theoretical model consists of three diffusion equations with biochemical reactions for dissolved oxygen (DO), phosphate and ferrous iron. According to this model, step changes in the DO concentration and flow velocity produce drastic changes in the SOD and phosphate release rate within 10 minutes. The vigorous response of the SOD and phosphate release rate is caused by the difference in the time scale of diffusion in the water boundary layer and that of the biochemical reactions in the sediment. Secondly, a negative phosphate transfer from water to sediment can even occur under aerobic conditions. This is caused by the decrease in phosphate concentration in the aerobic layer due to adsorption.


2021 ◽  
Vol 13 (3) ◽  
pp. 1502
Author(s):  
Maria Xanthopoulou ◽  
Dimitrios Giliopoulos ◽  
Nikolaos Tzollas ◽  
Konstantinos S. Triantafyllidis ◽  
Margaritis Kostoglou ◽  
...  

In water and wastewater, phosphate anions are considered critical contaminants because they cause algae blooms and eutrophication. The present work aims at studying the removal of phosphate anions from aqueous solutions using silica particles functionalized with polyethylenimine. The parameters affecting the adsorption process such as pH, initial concentration, adsorbent dose, and the presence of competitive anions, such as carbonate, nitrate, sulfate and chromate ions, were studied. Equilibrium studies were carried out to determine their sorption capacity and the rate of phosphate ions uptake. The adsorption isotherm data fitted well with the Langmuir and Sips model. The maximum sorption capacity was 41.1 mg/g at pH 5, which decreased slightly at pH 7. The efficiency of phosphate removal adsorption increased at lower pH values and by increasing the adsorbent dose. The maximum phosphate removal was 80% for pH 5 and decreased to 75% for pH 6, to 73% for pH 7 and to 70% for pH 8, for initial phosphate concentration at about 1 mg/L and for a dose of adsorbent 100 mg/L. The removal rate was increased with the increase of the adsorbent dose. For example, for initial phosphate concentration of 4 mg/L the removal rate increased from 40% to 80% by increasing the dose from 0.1 to 2.0 g/L at pH 7. The competitive anions adversely affected phosphate removal. Though they were also found to be removed to a certain extent. Their co-removal provided an adsorbent which might be very useful for treating waters with low-level multiple contaminant occurrence in natural or engineered aquatic systems.


2021 ◽  
pp. 1-10
Author(s):  
Weichen Zhang ◽  
Qiuna Du ◽  
Jing Xiao ◽  
Zhaori Bi ◽  
Chen Yu ◽  
...  

<b><i>Background:</i></b> Our research group has previously reported a noninvasive model that estimates phosphate removal within a 4-h hemodialysis (HD) treatment. The aim of this study was to modify the original model and validate the accuracy of the new model of phosphate removal for HD and hemodiafiltration (HDF) treatment. <b><i>Methods:</i></b> A total of 109 HD patients from 3 HD centers were enrolled. The actual phosphate removal amount was calculated using the area under the dialysate phosphate concentration time curve. Model modification was executed using second-order multivariable polynomial regression analysis to obtain a new parameter for dialyzer phosphate clearance. Bias, precision, and accuracy were measured in the internal and external validation to determine the performance of the modified model. <b><i>Results:</i></b> Mean age of the enrolled patients was 63 ± 12 years, and 67 (61.5%) were male. Phosphate removal was 19.06 ± 8.12 mmol and 17.38 ± 6.75 mmol in 4-h HD and HDF treatments, respectively, with no significant difference. The modified phosphate removal model was expressed as Tpo<sub>4</sub> = 80.3 × <i>C</i><sub>45</sub> − 0.024 × age + 0.07 × weight + β × clearance − 8.14 (β = 6.231 × 10<sup>−3</sup> × clearance − 1.886 × 10<sup>−5</sup> × clearance<sup>2</sup> – 0.467), where <i>C</i><sub>45</sub> was the phosphate concentration in the spent dialysate measured at the 45th minute of HD and clearance was the phosphate clearance of the dialyzer. Internal validation indicated that the new model was superior to the original model with a significantly smaller bias and higher accuracy. External validation showed that <i>R</i><sup>2</sup>, bias, and accuracy were not significantly different than those of internal validation. <b><i>Conclusions:</i></b> A new model was generated to quantify phosphate removal by 4-h HD and HDF with a dialyzer surface area of 1.3–1.8 m<sup>2</sup>. This modified model would contribute to the evaluation of phosphate balance and individualized therapy of hyperphosphatemia.


1980 ◽  
Vol 238 (1) ◽  
pp. F31-F36 ◽  
Author(s):  
J. P. Johnson ◽  
S. Green ◽  
J. H. Schwartz

The effects of changes in pH and addition of CO2/HCO3- on transepithelial phosphate transport were studied in turtle urinary bladder. Net mucosa-to-serosa flux of phosphate (JP) was determined as the difference between unidirectional 32P fluxes in the absence of transepithelial electrochemical gradients. With 5 mM phosphate in HCO3--free Ringer at pH 8.4, JP was 21.8 +/- 7.4 nmol . 8 cm-2 . h-1. There was a slight increase in JP with isohydric addition of 10 mM HCO3-. Addition of 5% CO2, which reduced pH to 7.3, did not affect JP. At pH 8.4, JP was not affected by ouabain or dinitrophenol and increased progressively as phosphate concentration was raised between 0.5 and 10 mM. At pH 6.2 in the absence of exogenous CO2 and HCO3-, JP was undectable. With 2.5 mM HCO3- and 5% CO2 at pH 6.5, JP was 61.3 +/- 16.0 and decreased to 30.6 +/- 1.6 nmol . 8 cm-2 . h-1 when pH was raised to 7.2 by increasing HCO3- to 10 mM. At pH 6.5 JP was inhibited by both ouabain and dinitrophenol. These results suggest that at acidic pH, JP results from the tranport of H2PO4-. The transport of H2PO4- is CO2 dependent and inhibited by ouabain and dinitrophenol. In contrast, at alkaline pH, JP results from the transport of HPO4(2-), which is neither CO2 dependent nor inhibited by ouabain or dinitrophenol.


2015 ◽  
Vol 35 (7) ◽  
pp. 637-642 ◽  
Author(s):  
Daisuke Kobayashi ◽  
Teruki Yoshimura ◽  
Atsushi Johno ◽  
Mika Ishikawa ◽  
Keiko Sasaki ◽  
...  

1968 ◽  
Vol 106 (3) ◽  
pp. 581-586 ◽  
Author(s):  
T. R. C. Boyde

1. The Michaelis constants for both isoenzymes for both substrates depend strongly on ionic concentration, being approximately proportional to phosphate concentration over considerable ranges. This is probably an effect of anions only. 2. In the absence of added salt, Km (2-oxoglutarate) (anionic isoenzyme) is so small as to be indeterminate. 3. Km (l-aspartate) (anionic isoenzyme) passes through a sharp minimum at about 3·3mm-phosphate. It is not clear whether this is a specific effect of phosphate. 4. Both substrates are inhibitory at sufficiently low ionic concentrations. 5. A modified graphical procedure is described for the derivation of the kinetic constants.


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