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Highlights • Solubilities of the K+, NH 4 +//Cl−, SO 4 2− - H 2 O system were measured by isothermal method. • Completed determination of solid solution composition based on the linear rule. • A technological process to produce chlorine-free K-N compound fertilizers and by-product potassium ammonium chloride. • The proposed process was verified by experiments. Abstract In order to produce chloride-free K-N compound fertilizers by the reaction of KCl (carnallite) and (NH 4) 2 SO 4 as raw materials, the phase equilibrium of the mutual quaternary system K+, NH 4 +//Cl−, SO 4 2− - H 2 O and its two ternary subsystems KCl-NH 4 Cl-H 2 O, K 2 SO 4 -(NH 4) 2 SO 4 -H 2 O were measured by isothermal method at 273.15 K. And the corresponding phase diagrams were plotted and analysed. The equilibrium phase diagram of the quaternary system K+, NH 4 +//Cl−, SO 4 2− - H 2 O shows that there is one saturation point and three solid phase fields of crystallization. Three fields of crystallization represent solid solution salts corresponding to (K 1−t , (NH 4) t) 2 SO 4, (K 1−m , (NH 4) m)Cl and ((NH 4) n , K 1−n)Cl respectively. The phase analysis shows that field of (K 1−t , (NH 4) t) 2 SO 4 is larger than other crystalline fields, and there is no crystalline field of pure potassium sulfate, which indicates that the K 1-t, (NH 4) t) 2 SO 4 is easy to crystallize out from solution. By analysing and calculating the phase diagrams of K+, NH 4 +//Cl−, SO 4 2− - H 2 O at 273.15 K and 323.15 K, chloride-free K-N compound fertilizers (K 1−t, (NH 4) t) 2 SO 4) can be obtained using KCl and (NH 4) 2 SO 4 as raw materials at 273.15 K, and ((NH 4) t , K 1−t)Cl can crystallize out at 323.15 K. The new technology shows the advantages of effective utilization of carnallite resources. The research on this quaternary phase diagram is the foundation of the chloride-free potash production by the reaction of carnallite and ammonium sulfate. [ABSTRACT FROM AUTHOR]

Solubilities of the quaternary system CO(NH 2 ) 2 -MgSO 4 -(NH 4 ) 2 SO 4 -H 2 O at 0 °C and 25 °C were studied by isothermal solution saturation method. Under the experimental data, phase diagrams were constructed. This quaternary system at 25 °C contains five crystallization regions corresponding to MgSO 4 ·7H 2 O, MgSO 4 ·(NH 4 ) 2 SO 4 ·6H 2 O, CO(NH 2 ) 2 , (NH 4 ) 2 SO 4 and MgSO 4 ·CO(NH 2 ) 2 ·2H 2 O. Compared with the phase diagram at 25 °C, there was no crystallization region of MgSO 4 ·CO(NH 2 ) 2 ·2H 2 O in the phase diagram at 0 °C·MgSO 4 ·(NH 4 ) 2 SO 4 ·6H 2 O has the largest crystallization area among the salts, indicating MgSO 4 ·(NH 4 ) 2 SO 4 ·6H 2 O is the easiest to crystallize out. Based on the characteristic of the phase diagrams, a new technology to separate (NH 4 ) 2 SO 4 and CO(NH 2 ) 2 from urea waste water is proposed. This process shows the advantages of recovering desirable substances and making urea waste water discharged up to standard. [ABSTRACT FROM AUTHOR]

• Solubilities of quaternary system NaCl-MgCl 2 -NH 4 Cl-H 2 O at 348.15 K. • The extended Pitzer model was used to predict the phase equilibrium data. • The ion interaction parameters θ and ψ at 348.15 K were regressed and calculated. • An optimized process to produce ammonium carnallite. Based on the requirement of the new technology to achieve comprehensive utilization of sodium and magnesium resources by using the mother solution from the preparation of potassium salt as raw material, the phase equilibrium data of the quaternary system NH 4 Cl-MgCl 2 -NaCl-H 2 O as well as its ternary subsystems MgCl 2 -NH 4 Cl-H 2 O and NaCl-NH 4 Cl-H 2 O were investigated by an isothermal equilibrium method under atmospheric pressure at 348.15 K, and the dry-salt phase diagram and water-phase diagram were drawn. Two invariant points and four crystallization fields including two single salts NH 4 Cl and NaCl, one hydrate salt MgCl 2 ·6H 2 O, and one double salt MgCl 2 ·NH 4 Cl·6H 2 O were determined in this quaternary system. Combining our results with available experimental data in the literature, an optimized process to produce ammonium carnallite and NaCl was proposed. Using the Pitzer electrolyte solution model, the experimental results were regressed and calculated. The calculated values agree well with the experimental values. [ABSTRACT FROM AUTHOR]

The stable phase equilibrium data of Mg2+, NH 4 +//Cl−, SO 4 2−−H 2 O quaternary interaction system and its four ternary subsystems at 363.15 K were determined by isothermal dissolution equilibrium method, and the corresponding stable phase diagrams of the above systems were plotted. According to the phase diagram, there are seven solid phase crystalline regions, which correspond to MgSO 4 ·(NH 4) 2 SO 4 ·6H 2 O, MgSO 4 ·6H 2 O, MgSO 4 ·4H 2 O, MgCl 2 ·6H 2 O, (NH 4) 2 SO 4 , MgCl 2 ·NH 4 Cl·6H 2 O and NH 4 Cl, respectively. MgSO 4 ·(NH 4) 2 SO 4 ·6H 2 O has the largest crystalline region among these crystalline regions, which indicates that the double salt MgSO 4 ·(NH 4) 2 SO 4 ·6H 2 O is the easiest to crystallize out. Based on the extended Pitzer model, the solubility data of the ternary subsystems and the quaternary system were calculated. The results showed that the calculated values were close to the experimental values. According to the comparison between the stable phase diagram of the quaternary system at 298.15 K and 363.15 K, a new process of preparing N–Mg compound fertilizer (MgSO 4 ·(NH 4) 2 SO 4 ·6H 2 O) at 298.15 K and crystallizing NH 4 Cl at 363.15 K by using ammonium sulfate and magnesium chloride as raw materials was designed in this paper and the process route was verified by experiment. [ABSTRACT FROM AUTHOR]

• Solubilities of NaCl-MgCl 2 -NH 4 Cl-H 2 O and its ternary subsystem NaCl-MgCl 2 -H 2 O were investigated. • The extended Pitzer model was applied to the phase equilibrium calculation. • The ion interaction parameters θ and ψ were correlated. • A technological process to produce ammonium carnallite and NaCl via mixed solution after extracting potassium chloride. Based on the requirement of the new technology for producing ammonium carnallite and NaCl via the solution left after the preparation of potassium salt as raw materials, the solubilities of the quaternary system NaCl-MgCl 2 -NH 4 Cl-H 2 O and ternary subsystem NaCl-MgCl 2 -H 2 O at 333.15 K were measured using the isothermal dissolution method, and the corresponding phase diagrams were plotted. The phase diagram of the ternary system consists of three fields of crystallization, which correspond to NaCl, MgCl 2 ·6H 2 O and their co-existing fields respectively. There are four fields of crystallization in the quaternary system, which correspond to MgCl 2 ·6H 2 O, NH 4 Cl, NaCl and the double salt MgCl 2 ·NH 4 Cl·6H 2 O respectively. By analyzing and calculating the phase diagrams, a technological route was proposed, which indicated that the Na-Mg resources were fully utilized. The extended Pitzer model was applied to the phase equilibrium calculation and the results showed that the calculated data were consistent with experimental values well. [ABSTRACT FROM AUTHOR]

Based on the requirement of the new technology for producing chloride-free potassium fertilizers by the reaction of KCl·MgCl 2 ·6H 2 O and (NH 4) 2 SO 4 , the phase equilibrium of the mutual quinary system K+, NH 4 +, Mg2+//SO 4 2−, Cl−- H 2 O at 273.15 K and 298.15 K were studied using the isothermal dissolution equilibrium method under atmospheric pressure, and the corresponding phase diagrams were plotted. According to the diagrams, there are seven saturation points and eight solid phase crystalline fields. Fields of K 2 SO 4 ·MgSO 4 ·6H 2 O and (NH 4u ,K 1-u) 2 SO 4 ·MgSO 4 ·6H 2 O are larger than other crystalline fields, which indicates that these two salts can crystallize out from solution easily. By analyzing and calculating the phase diagrams at 273.15 K and 298.15 K, chloride-free compound fertilizers can be produced via KCl·MgCl 2 ·6H 2 O and (NH 4) 2 SO 4 as raw materials, and the by-product NH 4 Cl can crystallize out. Image 1 • Solubilities of the quinary system K+, NH 4 +, Mg2+//SO 4 2−, Cl−- H 2 O were measured by isothermal method. • A technological process to produce chloride-free compound fertilizers and by-product ammonium chloride. • The proposed process was calculated theoretically and verified by experiment. [ABSTRACT FROM AUTHOR]