SDS Volume (2850)

Volume 66. Ammonium Phosphates, p None

Original Measurements

Sarbaev, A. N.; Polyakov, E. V.; Tyunina, M. F.; Polyakova, Z. A.; Ruchkova, A. Kh.; Khim. Prom. (Moscow) 1972, 48, 597-561.

Variables:

Composition, temperature and boiling points at pressures of 20 mm - 760 mm Hg of samples containing a N:P:K ratio equal - 1:1:1.

Prepared by:

J. Eysseltová

Method/Apparatus/Procedure:

A visual polythermic method was used at temperatures below 50 °C. Supersaturation was prevented by seeding. Above 50 °C a synthetic method was used [1-3]. The samples were placed in glass ampules and placed in an air thermostat where they were rotated at 3 rpm. They were observed through a glass window in the thermostat. A self-constructed apparatus based on the principle described elsewhere [4] was used.

Source and Purity of Materials:
  1. Reagent grade $\ce{NH4H2PO4}$ (GOST 6691-67) and urea (GOST 3771-64) and chemically pure KCl (GOST 4234-69) were used.
Estimated Errors:

Ambient temperature: With the visual-polythermic method the difference between the temperature of dissolution of the last crystal and appearance of the first crystal was less than + 0.5 K. Above 50°C the temperature had a precision of 0.4 K. No other information is given.
Mass concentration (m/v) (1): No information is given.

References

1 Alekseev, V. F.; Zh. Russ. Fiz. -Khim. Obshch. 1876, 8, 329.
2 Lebedeva, E. S.; Khodeeva, S. M. Zh. Fiz. Khim. 1961, 35, 2602.
3 Krichevskiy, I. R.; Khazanova, N. E.; Liushic, L. R.; Zh. Fiz. Khim. 1957, 31, 2711.
4 Goroletskiy, Ya; Olevskiy, V. M.; Levitanayte, R. P.; Zh. Fiz. Khim. 1964, 38, 2874.

Components:
  1. Ammonium dihydrogenphosphate, $\ce{ NH4H2PO4 }$; [7722-76-1] NIST WebBook
  2. Urea, $\ce{ CH4N2O }$; [57-13-6] NIST WebBook
  3. Potassium chloride, $\ce{ KCl }$; [7447-40-7] NIST WebBook
  4. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
Part 2. Composition and boiling points of saturated solutions in the NH4H2PO4-CO(NH2)2-KCl-H2O system at the ratio N:P:K = 1:1:1.
$P_{1}$ (mm Hg) 100w1 100w2 100w3 100w4 100w5 BP (°C) m2 (mol/kg) m3 (mol/kg) m4 (mol/kg)
20 31.95.5217.48.9568.1 26.71.352.231.76
50 36.66.3320.010.363.4 41.81.662.742.17
100 41.27.1322.511.658.8 56.92.023.332.64
150 44.27.6524.212.455.8 65.72.283.762.98
200 47.08.1325.713.253.0 73.02.554.213.34
250 49.08.4826.813.751.0 78.72.774.563.62
300 50.98.8127.814.349.1 83.62.994.923.90
350 52.69.1028.714.847.4 87.93.205.274.18
400 54.29.3829.615.245.8 91.83.415.624.45
450 55.79.6430.415.644.3 95.43.625.974.73
500 56.99.8431.116.043.1 98.53.806.274.97
550 57.910.031.616.242.1 100.93.966.535.18
600 59.110.232.316.640.9 103.64.166.865.44
650 60.010.432.816.840.0 105.74.327.125.65
700 61.010.633.317.139.0 108.04.507.435.89
760 62.210.834.017.537.8 110.64.747.826.19

(a) These values were calculated by the compiler. The molalities are expressed as mol/kg H2O.

(a) These values were calculated by the compiler. The molalities are expressed as mol/kg H2O.

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