AUSTHERM Pty Ltd
A.B.N. 83 066 556 661
Thermochemistry System
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The CSIRO-Monash Thermochemistry System Version 1, developed
at Monash University Department of Chemical Engineering, was
released in 1992. Version 2, also developed at Monash
University, was colour enhanced and initially developed in
1995 but never generally released.
MONASH THERMOCHEMISTRY System Version 1 and 2
ALL PROGRAMS
Program SYSTEM
Programs REACT and FILER
DATABANKS
A Gibbs energy databank of 3132 data sets for aqueous,
gaseous, liquid and solid species at a temperature of 25 C
has been created from NBS publications. The data may be
searched by name as well as by chemical formula.
A number of additional databank heat capacity relation
formats are available. These allow the user to directly
incorporate much of the data available in the published
literature.
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THE THERMOCHEMISTRY SYSTEM
Additional Features over CSIRO Thermochemistry System Version 5.1
Program CHEMIX
No help is given if not required. Information is given in
return for a "?" input or given automatically if requested.
On-line menus are available to operate the programs
interactively. A description is provided of each input. The
required format of the input is described. Examples of
input are provided from the HELP files. The information
required to define a system is listed. Command names can
either be entered in full or truncated.
Output may be regulated by time or by page for fast
computers or may be left unregulated.
Output lost off the screen during interactive operation may
be recalled from a buffer.
Mixed upper and lower case input may be optionally used to
provide more natural input of chemical formulae.
Element symbols are checked after each formula is input so
that a complete system does not have to be re-entered after
a simple error. Non-standard element symbols are available
to be defined as macros.
Frequently used chemical formula groupings, such as ligands,
may be replaced by macros.
The component basis is now automatically calculated by the
programs. This eliminates a major cause of program failure
in equilibrium and phase diagram calculation and reaction
balancing.
The chemical system currently in memory may be saved in
input file form for future use, thus allowing an interactive
session to be suspended then restarted.
A mathematical calculator is now accessible by the programs.
The user is given access to selected program variables
through the calculator. The calculator also allows the
input of mathematical expressions rather the constant values
in many program options, thus allowing almost infinite
program flexibility.
Alternate default units may be stored so that the programs
automatically use preferred units. Additional energy and
temperature units have been added.
Substitute command added to line editor.
A task related index and other new documentation is
provided.
The programs will operate in DOS on computers with extended
memory.
In-line comments can be placed after the " ; " symbol
Five new data set types are available:
USGS (type CPA)
Yaws/JANAF (type CPB)
Berman/Brown (type CPC)
Criss-Cobble/Helgeson (type CCH)
DIPPR (type DIP)
This allows direct data entry or creation of data banks by
the user from many published compilations.
The data currently in memory may be appended to data files
from all programs.
Graphical output may now be directly displayed without
additional software.
Plot points may be stored in an ASCII file for use by
spreadsheet or other programs
Output formats have been improved by eliminating leading and
trailing zeros in floating format eliminating trailing
decimal points centring or left justifying numbers where
appropriate
Old files are saved as backups if an attempt is made to
over-write them.
Unnecessary keystrokes have been eliminated from program
input.
Extra examples of the use of the system have been added.
The mass distribution of species in the equilibrium system
can be calculated.
The volume distribution between phases and species and the
density of the equilibrium system can be calculated.
General Activity Coefficient Model (user defined
expressions) Redlich-Kwong-Soave and Peng-Robinson Equations
of State
A system may be defined by specifying its chemical elements.
A System may be altered by adding or deleting phases and species.
The staged reactor option now allows different stage temperatures.
Non-Equilibrium calculations are now possible.
The K-values of species between phases may be calculated.
The user is warned of potentially incompatible phase combinations.
The user is warned if impossible constraints are placed on a system.
The user is warned if incompatible axes species are chosen.
Overlay lines may be optionally truncated and the overlay
line labelling is now optional
The activities of all species may be calculated for given
ordinate and abscissa values.