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70 MPa: 20 : 1. 9 281 266 125 51.

Chemours has taken the traditional paper pressure temperature (P/T) chart used for years and adapted it for today's technology.

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Enthalpy. 0. .

1 64 9.

. R452B is the closest drop-in equivalent to R410A in terms of capacity and efficiency. 9 281 266 125 51.

0 197 184 100 37. Store cylinders in a cool, dry, well-ventilated area, out of direct sunlight.

Critical temperature 78.

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Advantage assumes no responsibililty or liabilitly for data errors. Our Pressure Temperature Chart for the selected refrigerant is available for quick access; just use the button labeled (P/T).

Choose a fluid to model: Step 2. 31446261815324 × 250 / 101300 = 0.

7) Production of R-500 was halted by the clean air act on January 1, 1996.
com/Describes a Rankine power cycle with steam using a log pressure versus enthalpy diagram.
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Calculate online thermodynamic properties of moist (humid) air based on Hyland and Wexler formulation approved by American Society of Heating, Refrigeration and Air-conditioning Engineers.

Temperature and pressure chart for refrigerants R22, R410A, R12, R134A, R401A, R409A, R502, R404A, R507A, R408A and R402A.

Properties and characteristics Table 1: Comparisons between R32 and R410A PROPERTIES R32 R410A Boiling point -51. 7) Production of R-500 was halted by the clean air act on January 1, 1996. 7 156 144 85 29.

Yokozeki. The pressure-enthalpy diagram (log P/h diagram) is a very useful tool for refrigerant technicians, engineers and researchers. R134a. <span class=" fc-falcon">R32¶ References¶ Equation of State¶ R. Also, this has Temperature Glide ( T GL) of 0.

R-32 has GWP of 675, which is 68% lower than R-410A.

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Calculate pressure, volume, quantity (moles) or temperature of a gas with this versatile Ideal Gas Laws calculator (moles) by entering the other three.

r22 r134a r407c r404a r410a r507c sp22 r32 kpa psig kpa psig kpa psig kpa psig kpa psig kpa psig kpa psig kpa psig-30 63 9.

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It was confirmed that the temperature of pure R32, calculated by interpolating the measured temperatures at the inlet and outlet of test section, agreed well with the temperature calculated from the state of equation within 0.

0 364 350 145 62.