1994
DOI: 10.1039/ft9949001875
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Thermodynamic properties of 0–6 mol kg–1aqueous sulfuric acid from 273.15 to 328.15 K

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Cited by 210 publications
(357 citation statements)
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References 102 publications
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“…Acid errors were not an obvious problem as indicated by reproducible readings in the negative pH range although there was an initial adjustment necessary when changing to solutions of higher acid concentration. After completion of the field work, the response of the pH electrode assembly was assessed by The Pitzer model (20,(23)(24)(25) was used to calculate the theoretical pH of the prepared standard solutions. If the unscaled Pitzer approach is used, pH values for sulfuric acid solutions begin to diverge from MacInnes scaled values at pH values below -0.5.…”
Section: Methodsmentioning
confidence: 99%
“…Acid errors were not an obvious problem as indicated by reproducible readings in the negative pH range although there was an initial adjustment necessary when changing to solutions of higher acid concentration. After completion of the field work, the response of the pH electrode assembly was assessed by The Pitzer model (20,(23)(24)(25) was used to calculate the theoretical pH of the prepared standard solutions. If the unscaled Pitzer approach is used, pH values for sulfuric acid solutions begin to diverge from MacInnes scaled values at pH values below -0.5.…”
Section: Methodsmentioning
confidence: 99%
“…The thermochemical data for H 2 SO 4 /H 2 O uptake and loss by large aerosol particles derive from the liquid drop model and H 2 SO 4 and H 2 O vapour pressures over bulk solutions, calculated with a computer code (S. L. Clegg, personal communication, 2007) that is based on Giauque et al (1960);Clegg et al (1994). The thermochemical data for uptake/loss of gas phase H 2 SO 4 and H 2 O by intermediate sized particles are a smooth interpolation of the data for the small and large particles (see Lovejoy et al, 2004;.…”
Section: Maiamentioning
confidence: 99%
“…The parameters at 298.15 K given in their errata are listed in our Table 3, and were used to calculate values of φ at the 6 experimental concentrations reported in Table 1. were recalculated for consistency using up-to-date ion-interaction models for these reference standards [8][9][10]34], where the CaCl 2 (aq) model of Pitzer et al [10] is based on refitting of results from the critical assessment of Rard and Clegg [41]. Rard and Miller [30,39] generally used two or three isopiestic standards in their isopiestic measurements and the average value of the osmotic coefficient for MgCl 2 (aq) was accepted for each equilibration.…”
Section: Extended Ion-interaction Model Equations For Solutions Of Simentioning
confidence: 99%
“…The general equations for the extended ion-interaction for mixed electrolytes are given in Appendix I of reference [9]. …”
Section: Extended Ion-interaction Model Equations and Calculations Fomentioning
confidence: 99%
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