Research Article

Phase Equilibrium and Crystallization Process of the Ternary System KCl-(NH2)2CO-H2O at Different Temperatures

Table 3

Phase equilibrium data of the system KCl-(NH2)2CO-H2O at 303.15 K, 323.15 K, 333.15 K, and 343.15 Ka.

NumberEquilibrium solid phasecExperimental value/(/%)bCalculated value/(w/%)
Composition of liquid phaseComposition of wet solid phaseWilson modelNRTL model
KCl(NH2)2COKCl(NH2)2COKCl(NH2)2COKCl(NH2)2CO

303.15 K
1, M1P c27.320.00NDdND27.17e27.32
2P26.594.4263.081.2126.0626.28
3, A1P25.107.0668.042.2525.3325.50
4P23.7313.6771.613.9323.6523.65
5P20.6723.8764.259.6321.0220.71
6P18.3032.4766.0612.7818.8118.42
7P16.6741.1959.1519.8816.5416.37
8P15.5045.6161.9621.8015.4015.40
9P15.4147.4163.7920.3614.9015.04
10P14.2349.6865.6219.2514.3614.54
11, E1P+U13.9651.1459.9024.6413.9749.6114.2651.24
12U13.3552.409.4068.5450.1152.02
13U7.5953.756.4666.2752.9553.96
14, B1U4.1555.672.3965.3354.8655.59
15U1.8856.510.9076.2156.0256.50
16, N1U0.0057.01NDND56.9157.15
RAD1.58 × 10−20.93 × 10−2
RMSD0.800.24

323.15 K
1, M2P29.940.00NDND30.0630.00
2, A2P28.565.8963.493.7228.3628.32
3P26.3212.7773.224.4126.3326.36
4P23.4722.5369.239.0323.4623.62
5P21.6129.2362.7515.0821.4921.73
6P19.1538.9453.0222.5118.6018.92
7P18.0041.2062.4119.4517.9618.32
8P15.6150.5156.4225.8515.1815.49
9P14.5453.5944.1234.3514.2814.56
10P13.7056.7667.1818.9613.3313.54
11P13.1058.1155.0630.5812.9513.15
12, E2P+U12.4960.1551.5232.3912.3559.1412.4960.68
13U11.9761.559.4867.7359.6561.42
14U10.3762.787.6569.7460.8062.39
15U8.3663.215.4975.1561.9263.13
16, B2U5.8564.564.2869.4263.5364.41
17U2.3265.531.4377.9965.4765.78
18, N2U0.0067.35NDND67.1467.26
RAD1.59 × 10−20.69 × 10−2
RMSD0.830.21

333.15 K
1, M3P31.430.00NDND31.4031.08
2, A3P28.657.9372.152.4028.9428.62
3P26.3213.5072.115.0527.2126.92
4P24.1223.4366.0811.0224.2023.98
5P22.3229.0772.959.4622.4822.32
6P20.2335.8270.1214.3220.4020.32
7P18.6042.3568.715.4618.3718.32
8P16.6047.0567.9316.7916.9716.97
9P15.1952.3862.9524.0515.3115.27
10P13.9756.8163.7323.9413.9213.81
11, E3P+U11.8563.3962.5927.4811.9063.2411.6363.98
12U9.7865.359.6069.2864.8765.32
13U7.0967.125.9275.5466.7567.00
14, B3U4.8669.313.0877.4968.5868.70
15U2.7070.192.3581.8569.9069.84
16, N3U0.0071.25NDND71.4971.23
RAD0.92 × 10−20.90 × 10−2
RMSD0.370.32

343.15 K
1, M4P32.620.00NDND32.6231.95
2, A4P30.176.3777.772.4430.5729.87
3P27.7111.8078.884.3928.8128.16
4P25.1320.7468.87.5326.0125.44
5P22.4928.5860.6113.0123.5423.10
6P21.4333.2065.3913.7622.0821.69
7P19.5740.2264.3718.4319.8319.53
8P18.5843.8768.1118.0618.6518.38
9P15.2552.8462.6122.9515.8415.62
10P14.2655.9759.7526.4214.8414.60
11P12.9960.0269.5721.4413.5513.25
12P12.661.8862.1628.2712.9212.55
3P11.5965.3161.6127.1611.8111.33
14P11.1868.1569.8623.9210.7910.13
15, E4P+U10.2969.2760.2731.2510.5368.429.9169.79
16U9.1970.346.8078.6969.5370.26
17U7.7571.343.3182.2170.6071.21
18U5.9172.563.9488.7771.9572.41
19, B4U3.9773.411.8591.2673.1873.54
20U2.1974.780.8784.9174.5574.74
21, N4U0.0075.76NDND75.9275.94
RAD2.18 × 10−21.69 × 10−2
RMSD0.600.40

aStandard uncertainties u are u(T) = 0.1 K and ur(x) = 0.5%. b: mass fraction. cP: KCl; U: (NH2)2CO. dND: not determined. e—: the calculated value same as the experimental value.