Solid-liquid phase equilibrium for the system ammonium polyphosphate-urea ammonium nitrate-potassium chloride-water at 273.2 K
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Solid-liquid phase equilibrium for the system ammonium polyphosphate-urea ammonium nitrate-potassium chloride-water at 273.2 K
Solid-liquid phase equilibrium for the system ammonium polyphosphate-urea ammonium nitrate-potassium chloride-water at 273.2 K
中国化学工程学报(英文版)2023年60卷第8期 页码:131-142
Affiliations:
Ministry of Education Research Center for Comprehensive Utilization and Clean Processing Engineering of Phosphorus Resources, College of Chemical Engineering, Sichuan University,Chengdu,China,610065
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纸质出版:2023
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Xingjuan Liang, Dehua Xu, Zhengjuan Yan, 等. Solid-liquid phase equilibrium for the system ammonium polyphosphate-urea ammonium nitrate-potassium chloride-water at 273.2 K[J]. 中国化学工程学报(英文版), 2023,60(8):131-142.
Xingjuan Liang, Dehua Xu, Zhengjuan Yan, Jingxu Yang, Xinlong Wang, Zhiye Zhang, Jingli Wu, Honggang Zhen. Solid-liquid phase equilibrium for the system ammonium polyphosphate-urea ammonium nitrate-potassium chloride-water at 273.2 K[J]. Chinese Journal of Chemical Engineering, 2023, 60(8): 131-142.
Xingjuan Liang, Dehua Xu, Zhengjuan Yan, 等. Solid-liquid phase equilibrium for the system ammonium polyphosphate-urea ammonium nitrate-potassium chloride-water at 273.2 K[J]. 中国化学工程学报(英文版), 2023,60(8):131-142.DOI:
Xingjuan Liang, Dehua Xu, Zhengjuan Yan, Jingxu Yang, Xinlong Wang, Zhiye Zhang, Jingli Wu, Honggang Zhen. Solid-liquid phase equilibrium for the system ammonium polyphosphate-urea ammonium nitrate-potassium chloride-water at 273.2 K[J]. Chinese Journal of Chemical Engineering, 2023, 60(8): 131-142.DOI:
Solid-liquid phase equilibrium for the system ammonium polyphosphate-urea ammonium nitrate-potassium chloride-water at 273.2 K
a quaternary system of ammonium polyphosphate (APP)-urea ammonium nitrate (UAN
CO(NH
2
)
2
-NH
4
NO
3
)-potassium chloride (KCl)-H
2
O and its subsystems (APP-[CO(NH
2
)
2
-NH
4
NO
3
]
-H
2
O
KCl-[CO(NH
2
)
2
-NH
4
NO
3
]
-H
2
O and APP-KCl-H
2
O) were systematically investigated at the temperature of 273.2 K. Each ternary phase diagram contains one invariant point and three crystallization regions. The crystallization regions are: (1) (NH
4
)
3
HP
2
O
7
(NH
4
)
4
P
2
O
7
and ((NH
4
)
3
HP
2
O
7
+ (NH
4
)
4
P
2
O
7
) for APP-[CO(NH
2
)
2
-NH
4
NO
3
]
-H
2
O diagram; (2) KCl
KNO
3
and (KCl + KNO
3
) for KCl-[CO(NH
2
)
2
-NH
4
NO
3
]
-H
2
O diagram and (3) (NH
4
)
3
HP
2
O
7
KCl and ((NH
4
)
3
HP
2
O
7
+ KCl) for APP-KCl-H
2
O diagram. The quaternary phase diagram of APP-[CO(NH
2
)
2
-NH
4
NO
3
]
-KCl-H
2
O has no quaternary invariant point but includes four solid phase crystallization regions
i
.
e
.
(NH
4
)
3
HP
2
O
7
(NH
4
)
4
P
2
O
7
KNO
3
and KCl
in which the KNO
3
region occupies the largest area. The maximum total nutrient content (N + P
2
O
5
+ K
2
O) existing as ionic forms in the APP-[CO(NH
2
)
2
-NH
4
NO
3
]
-H
2
O
KCl-[CO(NH
2
)
2
-NH
4
NO
3
]
-H
2
O
APP-KCl-H
2
O and quaternary systems is 44.70%
32.86%
45.56% and 46.23% (mass)
respectively
indicating that the maximum nutrient content can be reached using raw materials of the corresponding systems to prepare liquid fertilizer. In the quaternary system
the content of ascends with the increase of the total nutrient content
while the contents of and CO(NH
2
)
2
-N increase with elevated total N. This work can help optimize the operating parameters for the production
storage and transportation of liquid fertilizers.
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references
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Separation of chlorineebromine-based solid solution in bittern tail solution by phase equilibrium
Solid-liquid phase equilibria in the aqueous system containing the chlorides of potassium, ammonium, and calcium at 298.2, 323.2, and 348.2 K
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