1997
DOI: 10.1006/jcht.1997.0230
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Measurement and correlation of the (p,ρ,T) relation of nitrogen. I. The homogeneous gas and liquid regions in the temperature range from 66 K to 340 K at pressures up to 12 MPa

Abstract: Measurement and correlation of the (p, r, T) relation of nitrogen I. The homogeneous gas and liquid regions in the temperature range from 66 K to 340 K at pressures up to 12 MPa P. Nowak, R. Kleinrahm, and W. Wagner

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Cited by 61 publications
(52 citation statements)
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“…Our data agree well with the literature data, and they exhibit considerably less scatter than the data of Ben et al [11] and Ejaz S. [12]. Ben et al [11]; +, Duschek et al [8]; ×,Nowak et al [9]; ,Ejaz S. [12].…”
Section: Comparing Experimental Results With Equation Of State and LIsupporting
confidence: 82%
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“…Our data agree well with the literature data, and they exhibit considerably less scatter than the data of Ben et al [11] and Ejaz S. [12]. Ben et al [11]; +, Duschek et al [8]; ×,Nowak et al [9]; ,Ejaz S. [12].…”
Section: Comparing Experimental Results With Equation Of State and LIsupporting
confidence: 82%
“…FIGURE 4 shows the comparison of the present experimental results with the literature data which overlap our temperature and pressure range. The data from Duschek et al [8] and Nowak et al [9] were measured by a two-sinker densimeter, and were used to fit the equation of Span et al [7]. The literature data [12] were measured by a single-sinker densimeter.…”
Section: Comparing Experimental Results With Equation Of State and LImentioning
confidence: 99%
“…These pressure differences, ranging from about 2.5 kPa to 0.2 kPa, were achieved by setting different filling levels above the sinkers. Then, the saturated-liquid density was determined by extrapolating these isothermal liquid densities to ( p − p s ) = 0, again by non-linearly fitting equation (1) to the ( p, r, T ) values.…”
Section: Methodsmentioning
confidence: 99%
“…In the critical region, however, the measurements were carried out in a way similar to FIGURE 1. Schematic illustration of the new procedure to determine the saturated-vapour densities very close (in this case at T = 126.170 K) to the critical temperature Tc = 126.192 K. A: filling of the measuring cell; B: Phase equilibrium (vapour + liquid) in the measuring cell; q, (p, r, T) measurements in the homogeneous gas region close to the phase boundary (vapour + liquid); w, (p, r, T) measurements in the homogeneous gas region extremely close to the phase boundary (vapour + liquid); these values were measured in a quasi-equilibrium state while the fluid in the measuring cell was slowly condensing; = w, ( p, r, T ) value measured after phase equilibrium (vapour + liquid) had been achieved in the measuring cell; (, saturated-vapour density r0 determined by extrapolating all measured ( p, r, T ) values in the gas-phase to ( p − ps ) = 0 by means of equation (1). Also, Dphyd corresponds to the hydrostatic pressure of the gas column between the phase boundary (vapour + liquid) a few mm above the bottom of the measuring cell and the reference height of the two sinkers (see figure 1 in reference 3); this distance only amounts to a few cm and is very well known.…”
Section: Methodsmentioning
confidence: 99%
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