Phase Equilibrium of NH_3-CO_2-H_2O-NH_2CONH_2 System at High Temperature and Pressure in Urea Synthesis
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Phase Equilibrium of NH_3-CO_2-H_2O-NH_2CONH_2 System at High Temperature and Pressure in Urea Synthesis
CIESC JournalIssue 6, (1990)
作者机构:
上海化工研究院,上海化工研究院,上海化工研究院 ,上海,上海,上海
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Online First:25 December 1990,
Published:25 December 1990
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Hu Liegi, Wei Boyi and Shen HuaminShanghai Research Institute of Chemical Industry, Shanghai. Phase Equilibrium of NH_3-CO_2-H_2O-NH_2CONH_2 System at High Temperature and Pressure in Urea Synthesis[J]. CIESC Journal, 1990, (6).
DOI:
Hu Liegi, Wei Boyi and Shen HuaminShanghai Research Institute of Chemical Industry, Shanghai. Phase Equilibrium of NH_3-CO_2-H_2O-NH_2CONH_2 System at High Temperature and Pressure in Urea Synthesis[J]. CIESC Journal, 1990, (6).DOI:
Phase Equilibrium of NH_3-CO_2-H_2O-NH_2CONH_2 System at High Temperature and Pressure in Urea Synthesis
A new thermodynamic model for ammonia-carbon dioxide-water-urea system at the condition of urea synthesis (T=438.15-478.15K
P=6.87-24.5 MPa
NH3/CO2 = 2.6-5.0
H2O/CO2= 0.2-1.2) is established on the basis of experimental data. Perturbed-hard-sphere equation of state and Wilson equation are use to treat the non-idealities of vapor and liquid phases. Correlations of the experimental data at 433.15K
438.15K
448.15K
458.15K
468.15K and 478.15K are made with this model. The mean relative deviation of molar fraction of ammonia and carbon dioxide in vapor phase is 3.05% and 8.27% respectively
and the mean relative deviation of total pressure is 3.31%. The calculated values of pressure with this mode] are in agreement with those of industrial synthesis of urea.