R-507A PT Chart

R-507A saturation pressure, −40 to 150 °F−40 to 65 °C. Used in low temperature commercial refrigeration.

How to use ↓

Safety class A1Azeotropic blendGlide 0.04 °F at 40 °F evap (negligible)Glide 0.02 K at 4.4 °C evap (negligible)

PT lookup

Step 2 I know the
°F°C

Type a temperature to see the saturation pressure.

R-507A pressure temperature table

Liquid = bubble (subcooling). Vapor = dew (superheat). Highlighted: 40 °F and 100 °F.Liquid = bubble (subcooling). Vapor = dew (superheat). Negative kPa = vacuum. Highlighted: 4 °C and 38 °C.

R-507A saturation pressure by temperature, °F and psig (vacuum in inches of mercury)
°FLiquid bubble, psigVapor dew, psig
-405.45.4
-395.95.9
-386.46.4
-377.07.0
-367.57.5
-358.18.1
-348.68.6
-339.29.2
-329.89.8
-3110.410.3
-3011.011.0
-2911.611.6
-2812.212.2
-2712.812.8
-2613.513.5
-2514.114.1
-2414.814.8
-2315.515.5
-2216.216.2
-2116.916.9
-2017.617.6
-1918.318.3
-1819.119.1
-1719.819.8
-1620.620.6
-1521.421.4
-1422.222.2
-1323.023.0
-1223.823.8
-1124.724.6
-1025.525.5
-926.426.4
-827.327.2
-728.228.1
-629.129.0
-530.030.0
-430.930.9
-331.931.9
-232.832.8
-133.833.8
034.834.8
135.835.8
236.936.8
337.937.9
439.038.9
540.140.0
641.141.1
742.342.2
843.443.4
944.544.5
1045.745.7
1146.946.8
1248.148.0
1349.349.2
1450.550.5
1551.851.7
1653.053.0
1754.354.3
1855.655.6
1956.956.9
2058.358.2
2159.659.6
2261.061.0
2362.462.4
2463.863.8
2565.365.2
2666.766.7
2768.268.1
2869.769.6
2971.271.1
3072.772.7
3174.374.2
3275.975.8
3377.577.4
3479.179.0
3580.780.7
3682.482.3
3784.184.0
3885.885.7
3987.587.4
4089.289.2
4191.090.9
4292.892.7
4394.694.6
4496.596.4
4598.398.3
46100.2100.1
47102.1102.0
48104.1104.0
49106.0105.9
50108.0107.9
51110.0109.9
52112.0111.9
53114.1114.0
54116.2116.1
55118.3118.2
56120.4120.3
57122.6122.5
58124.7124.6
59127.0126.8
60129.2129.1
61131.4131.3
62133.7133.6
63136.0135.9
64138.4138.3
65140.7140.6
66143.1143.0
67145.6145.4
68148.0147.9
69150.5150.3
70153.0152.8
71155.5155.4
72158.1157.9
73160.7160.5
74163.3163.1
75165.9165.8
76168.6168.5
77171.3171.2
78174.1173.9
79176.8176.7
80179.6179.5
81182.5182.3
82185.3185.1
83188.2188.0
84191.1190.9
85194.1193.9
86197.1196.9
87200.1199.9
88203.1202.9
89206.2206.0
90209.3209.1
91212.5212.3
92215.6215.4
93218.9218.7
94222.1221.9
95225.4225.2
96228.7228.5
97232.0231.8
98235.4235.2
99238.8238.6
100242.3242.1
101245.8245.6
102249.3249.1
103252.9252.6
104256.5256.2
105260.1259.9
106263.8263.5
107267.5267.2
108271.2271.0
109275.0274.8
110278.8278.6
111282.7282.4
112286.6286.3
113290.5290.3
114294.5294.2
115298.5298.3
116302.6302.3
117306.7306.4
118310.8310.5
119315.0314.7
120319.2318.9
121323.5323.2
122327.8327.5
123332.1331.8
124336.5336.2
125340.9340.7
126345.4345.1
127349.9349.7
128354.5354.2
129359.1358.8
130363.8363.5
131368.5368.2
132373.2372.9
133378.0377.7
134382.9382.6
135387.8387.5
136392.7392.4
137397.7397.4
138402.7402.4
139407.8407.5
140413.0412.7
141418.2417.9
142423.4423.1
143428.7428.4
144434.1433.8
145439.5439.2
146444.9444.7
147450.5450.2
148456.1455.8
149461.7461.5
150467.4467.2
R-507A saturation pressure by temperature, °C and kPa (negative = vacuum)
°CLiquid bubble, kPaVapor dew, kPa
-4037.337.3
-3943.743.7
-3850.350.3
-3757.157.1
-3664.164.1
-3571.471.4
-3478.978.9
-3386.786.6
-3294.794.7
-31103.0103.0
-30111.6111.5
-29120.4120.3
-28129.5129.5
-27138.9138.8
-26148.6148.5
-25158.6158.5
-24168.9168.8
-23179.5179.4
-22190.4190.3
-21201.6201.5
-20213.2213.1
-19225.1225.0
-18237.3237.2
-17249.9249.8
-16262.8262.7
-15276.1276.0
-14289.8289.6
-13303.8303.6
-12318.2318.0
-11333.0332.8
-10348.2348.0
-9363.8363.5
-8379.8379.5
-7396.2395.9
-6413.0412.7
-5430.2429.9
-4447.9447.6
-3466.0465.7
-2484.6484.2
-1503.6503.2
0523.1522.6
1543.0542.6
2563.4562.9
3584.3583.8
4605.7605.2
5627.6627.0
6649.9649.4
7672.8672.3
8696.3695.6
9720.2719.6
10744.7744.0
11769.7769.0
12795.2794.5
13821.4820.6
14848.1847.3
15875.3874.5
16903.2902.3
17931.6930.7
18960.6959.7
19990.3989.3
201020.51019.6
211051.41050.4
221082.91081.9
231115.01114.0
241147.81146.7
251181.31180.2
261215.41214.2
271250.21249.0
281285.61284.4
291321.81320.6
301358.71357.4
311396.31395.0
321434.61433.2
331473.61472.2
341513.41512.0
351553.91552.5
361595.21593.8
371637.31635.8
381680.21678.6
391723.81722.2
401768.31766.7
411813.61811.9
421859.71858.0
431906.61904.9
441954.41952.7
452003.12001.3
462052.62050.8
472103.12101.3
482154.42152.6
492206.72204.8
502259.92258.0
512314.02312.2
522369.22367.3
532425.32423.4
542482.42480.5
552540.52538.6
562599.72597.8
572659.92658.0
582721.32719.3
592783.72781.8
602847.32845.4
612912.02910.1
622978.02976.1
633045.13043.3
643113.63111.8
653183.43181.6
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R-507A PT Chart

°F / psig · Safety class A1 · Azeotropic blend

refrigerantptchart.com

°FLiquidVapor
-405.45.4
-395.95.9
-386.46.4
-377.07.0
-367.57.5
-358.18.1
-348.68.6
-339.29.2
-329.89.8
-3110.410.3
-3011.011.0
-2911.611.6
-2812.212.2
-2712.812.8
-2613.513.5
-2514.114.1
-2414.814.8
-2315.515.5
-2216.216.2
-2116.916.9
-2017.617.6
-1918.318.3
-1819.119.1
-1719.819.8
-1620.620.6
-1521.421.4
-1422.222.2
-1323.023.0
-1223.823.8
-1124.724.6
-1025.525.5
-926.426.4
-827.327.2
-728.228.1
-629.129.0
-530.030.0
-430.930.9
-331.931.9
-232.832.8
-133.833.8
034.834.8
135.835.8
236.936.8
337.937.9
439.038.9
540.140.0
641.141.1
742.342.2
°FLiquidVapor
843.443.4
944.544.5
1045.745.7
1146.946.8
1248.148.0
1349.349.2
1450.550.5
1551.851.7
1653.053.0
1754.354.3
1855.655.6
1956.956.9
2058.358.2
2159.659.6
2261.061.0
2362.462.4
2463.863.8
2565.365.2
2666.766.7
2768.268.1
2869.769.6
2971.271.1
3072.772.7
3174.374.2
3275.975.8
3377.577.4
3479.179.0
3580.780.7
3682.482.3
3784.184.0
3885.885.7
3987.587.4
4089.289.2
4191.090.9
4292.892.7
4394.694.6
4496.596.4
4598.398.3
46100.2100.1
47102.1102.0
48104.1104.0
49106.0105.9
50108.0107.9
51110.0109.9
52112.0111.9
53114.1114.0
54116.2116.1
55118.3118.2
°FLiquidVapor
56120.4120.3
57122.6122.5
58124.7124.6
59127.0126.8
60129.2129.1
61131.4131.3
62133.7133.6
63136.0135.9
64138.4138.3
65140.7140.6
66143.1143.0
67145.6145.4
68148.0147.9
69150.5150.3
70153.0152.8
71155.5155.4
72158.1157.9
73160.7160.5
74163.3163.1
75165.9165.8
76168.6168.5
77171.3171.2
78174.1173.9
79176.8176.7
80179.6179.5
81182.5182.3
82185.3185.1
83188.2188.0
84191.1190.9
85194.1193.9
86197.1196.9
87200.1199.9
88203.1202.9
89206.2206.0
90209.3209.1
91212.5212.3
92215.6215.4
93218.9218.7
94222.1221.9
95225.4225.2
96228.7228.5
97232.0231.8
98235.4235.2
99238.8238.6
100242.3242.1
101245.8245.6
102249.3249.1
103252.9252.6
°FLiquidVapor
104256.5256.2
105260.1259.9
106263.8263.5
107267.5267.2
108271.2271.0
109275.0274.8
110278.8278.6
111282.7282.4
112286.6286.3
113290.5290.3
114294.5294.2
115298.5298.3
116302.6302.3
117306.7306.4
118310.8310.5
119315.0314.7
120319.2318.9
121323.5323.2
122327.8327.5
123332.1331.8
124336.5336.2
125340.9340.7
126345.4345.1
127349.9349.7
128354.5354.2
129359.1358.8
130363.8363.5
131368.5368.2
132373.2372.9
133378.0377.7
134382.9382.6
135387.8387.5
136392.7392.4
137397.7397.4
138402.7402.4
139407.8407.5
140413.0412.7
141418.2417.9
142423.4423.1
143428.7428.4
144434.1433.8
145439.5439.2
146444.9444.7
147450.5450.2
148456.1455.8
149461.7461.5
150467.4467.2

Liquid = bubble (use for subcooling). Vapor = dew (use for superheat). Bold rows: 40 °F and 100 °F. Reference only: always verify with the manufacturer’s data and your gauges.

R-507A PT Chart

°C / kPa (gauge) · Safety class A1 · Azeotropic blend

refrigerantptchart.com

°CLiquidVapor
-4037.337.3
-3943.743.7
-3850.350.3
-3757.157.1
-3664.164.1
-3571.471.4
-3478.978.9
-3386.786.6
-3294.794.7
-31103.0103.0
-30111.6111.5
-29120.4120.3
-28129.5129.5
-27138.9138.8
-26148.6148.5
-25158.6158.5
-24168.9168.8
-23179.5179.4
-22190.4190.3
-21201.6201.5
-20213.2213.1
-19225.1225.0
-18237.3237.2
-17249.9249.8
-16262.8262.7
-15276.1276.0
-14289.8289.6
-13303.8303.6
-12318.2318.0
-11333.0332.8
-10348.2348.0
-9363.8363.5
-8379.8379.5
-7396.2395.9
-6413.0412.7
-5430.2429.9
°CLiquidVapor
-4447.9447.6
-3466.0465.7
-2484.6484.2
-1503.6503.2
0523.1522.6
1543.0542.6
2563.4562.9
3584.3583.8
4605.7605.2
5627.6627.0
6649.9649.4
7672.8672.3
8696.3695.6
9720.2719.6
10744.7744.0
11769.7769.0
12795.2794.5
13821.4820.6
14848.1847.3
15875.3874.5
16903.2902.3
17931.6930.7
18960.6959.7
19990.3989.3
201020.51019.6
211051.41050.4
221082.91081.9
231115.01114.0
241147.81146.7
251181.31180.2
261215.41214.2
271250.21249.0
281285.61284.4
291321.81320.6
301358.71357.4
311396.31395.0
°CLiquidVapor
321434.61433.2
331473.61472.2
341513.41512.0
351553.91552.5
361595.21593.8
371637.31635.8
381680.21678.6
391723.81722.2
401768.31766.7
411813.61811.9
421859.71858.0
431906.61904.9
441954.41952.7
452003.12001.3
462052.62050.8
472103.12101.3
482154.42152.6
492206.72204.8
502259.92258.0
512314.02312.2
522369.22367.3
532425.32423.4
542482.42480.5
552540.52538.6
562599.72597.8
572659.92658.0
582721.32719.3
592783.72781.8
602847.32845.4
612912.02910.1
622978.02976.1
633045.13043.3
643113.63111.8
653183.43181.6

Liquid = bubble (use for subcooling). Vapor = dew (use for superheat). Bold rows: 4 °C and 38 °C. Reference only: always verify with the manufacturer’s data and your gauges.

How to use

  1. Choose Temperature or Pressure and type the number. The answer shows straight away.
  2. Blends show two values: use vapor (dew) for superheat and liquid (bubble) for subcooling.
  3. Tap °C · kPa for metric. Below 0 psig, pressure is in inches of mercury (inHg) vacuum.
  4. Press Print pocket chart for a one-page chart (Letter or A4) for the van or the tool bag.

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About this R-507A chart

This R-507A pressure temperature chart gives the saturation pressure for every degree, in psig with °F or kPa (gauge) with °C. As a blend, it has a liquid (bubble) and a vapor (dew) column.

Source: manufacturer and supplier charts (Chemours, Honeywell, Arkema, A-Gas). Reference only: always verify with the manufacturer’s data and your gauges.

FAQ

What is the R-507A pressure at 40 °F?

89.2 psig vapor (dew) and 89.2 psig liquid (bubble) at saturation, from the table above.

What is the R-507A pressure at 100 °F?

242.1 psig vapor (dew) and 242.3 psig liquid (bubble) at saturation.

Why does R-507A have two columns?

R-507A is a blend with very little glide (0.04 °F), so liquid (bubble) and vapor (dew) are almost the same. Use vapor for superheat and liquid for subcooling.

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