HSC Chemistry, HSC Chemistry 7, Software for Process simulation, Reactions Equations, Heat and Material Balances, Equilibrium Calculations, Electrochemical Cell Equilibriums, Eh-pH Diagrams – Pourbaix diagram
 
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Modules
All modules included as standard

 Sim Process Simulation
 Reaction Equations
 Heat and Material Balances
 Heat Loss Calculator
 Equilibrium Calculations
 Electrochemical Cell Equilibriums
 Eh-pH Diagrams – Pourbaix
 H, S, C and Ellingham Diagrams
 Tpp Diagrams – Stability diagrams
 Lpp Diagrams – Stability diagrams
 Water – Steam tables, etc.
 H, S, Cp Estimates
 Conversions – Species to elements
 Mineralogy Iterations
 Periodic Chart – Elements
 Measure Units
 HSC Add-In Functions
 Data – Statistical Analysis
 Geo Mineralogical Calculations
 Map GPS material Stock
 Fit – Numerical Data Fit
 Aqueous Solution Property Estimator
 
Databases
All included as standard

HSC Thermochemical Database
Water Steam/Fluid Database
Heat Conduction Database
Heat Convection Database
Surface Radiation Database
Gas Radiation Calculator
Particle Radiation Calculator
Elements Database
Measure Units Database
Minerals Database
Aqueous Solution Density Database
The Pitzer parameter Database
  The Pitzer parameter Database

Well-known non-ideal models for aqueous electrolytes properties have been included in the new Aqua module. The activity coefficient models include the extended Debye-Hückel model here called Davies model, Pitzer model, and Harvie’s modification. An extensive database including about 1000 Pitzer parameters for different systems have been collected to date. The Pitzer parameter database currently has 407 cation-anion pairs, 102 cation-cation and anion-anion pairs, 114 ternary coefficients, and 289 ion-neutral pairs. Many of these parameters are tabulated as temperature-dependent functions.

 

The enthalpy of aqueous solutions and especially the activity coefficients depend on the concentrations of the species. The new Aqueous Estimator module provides you with an easy way to estimate activity coefficients, enthalpies and heat capacities of dilute, moderate, and concentrated electrolyte solutions as a first guess for process design purposes. These estimated values may be utilized in process models and other HSC calculation modules. At this point, only homogeneous liquid phases can be calculated, i.e. precipitated phases are not yet included. The user has to specify the temperature, species, compositions, and temperature of the water solution and the module estimates activity coefficients, enthalpies, and heat capacities.