To calculate pressure drops you need data of flow medium: Density and viscosity. In
these databases you will find properties of many liquids and gases. Besides you
can estimate properties.
Properties of
water/-steam (general)
Calculation of properties of water and steam according Industry Standard
IAPWS-IF 97. Calculations are possible within the range: 0 °C <= Temp.
<= 800 °C at pressure (abs.) <= 1000 bar 800 °C < Temp. <= 900 °C
bei pressure (abs.) <= 100 bar I you want calculate water at normal air
pressure input pressure value 1.013 bar.
Properties of
water/-steam (saturated)
Calculation of density and viscosity of water and steam in saturated
condition. In saturated condition (saturated steam, saturated liquid) is the
medium at boiling point. Calculation according Industry Standard IAPWS-IF 97
within the range: 0 to 373 °C
Properties of dry
air
Calculation of real gas properties of dry air (gaseous and liquid state) in
the range from 60 to 2000 K up to 20000 bar. The values are calculated data.
Small differences to reality are possible. If you want calculate air on
athmospheric pressure please use as pressure 1.013 bar.
Properties of humid air
Calculation of real gas properties of humid air in the range from 0 to 200 °C
up to 100 bar. The values are calculated data. Small differences to reality are
possible. If you want calculate air on athmospheric pressure please use as
pressure 1.013 bar.
Properties of air (saturated)
Calculation of real gas properties of air in saturated condition (saturated
steam and saturated liquid) in the range from 60 to 132 K.
Properties of CO2 (general)
Calculation of real gas properties of CO2 in the range from 216 to 1100 K up
to 8000 bar. The values are calculated data. Small differences to reality are
possible. If you want calculate CO2 on athmospheric pressure please use as
pressure 1.013 bar. Calculation of density according Span and Wagner,
calculation of viscosity according Fenghour and Wakeham.
Properties CO2 (saturated)
Calculation of real gas properties of CO2 in saturated condition (saturated
steam and saturated liquid) in the range from 217 to 304 K.
Properties of other liquids
In this database you will find data of diverse liquids. These data are
measurements no calculated data. Values between two measurements you can
interpolate.
Properties of
other gases
In this database you will find data of various gases at different pressures
and temperatures.
Viscosity: The viscosity values are measured values at atmospheric
pressure (1.013 bar). In the range of 0.1 - 10 bar the viscosity is not
dependent of pressure and is consequently not calculated If the pressure is
> 1.013 bar the changing of the viscosity is calculated with the formula of
Gardner. The error could be 5 to 10% if the molecules are uncomplex.
Density: The density values are calculated with the formula of
Redlich-Kwong-Soave. The results are very exact for real gases also.
Critical temperature: The critical temperature of a material is the
temperature above which unique liquid and gas phases do not exist. As the
critical temperature is approached, the properties of the gas and liquid phases
become the same. Above the critical temperature, there is only one phase.
Calculation of
properties
Calculation of density and viscosity of liquids, gases and mixtures. In
many cases are no measured values are available and have to be calculated. The
calculated properties are approximate values. If you need very exact data you
should use measured values. If you need exact data from Water, Air etc.
please use the separate menus.
You can here calculate refrigerants also.
The following errors are possible:
Gases Density: Very exact calculation Viscosity at atmospheric
pressure: Max. 4% (more if you calculate polar moleculs) Viscosity at
pressure > atmospheric: 5 to 10% (more if you calculate complex moleculs)
Liquids Density: Max. 3% Viscosity: Very exact calculation
The following formulas are used to calculate the properties:
Gases Density: Redlich-Kwong-Soave Viscosity: Rother und Gardner
Information to the calculation of mixtures (liquid-liquid or
gas-gas)
The calculated properties are approximate values. If you need very exact data
you should use measured values The viscosity calculation of mixtures is an
estimation.
The mixtures are calculated from the properties of the components acc. the
following formulas:
Gases Density: Amagat Viscosity: Mixture formula
Liquids: Density: Amagat Viscosity: Arrhenius
Calculation of aqueous solutions
You can calculate aqueous solutions in different concentrations at different
temperatures. It's also possible to calculate solutions with more than one
substance.
The calculated properties are approximate values. If you need very exact data
you should use measured values.
If you input unrealistic concentrations or temperatures above the boiling
point the program doesn't show an error message because the program doesn't
calculate solubilities/boiling points! Boiling points of aqueous solutions you
can calculate with our software Dampfdruck.
Calculation of liquid
refrigerants
Calculation of properties of liquid refrigerants (Glycol, Glycerol,
Ethanol...) at different temperatures and concentrations.
Calculation of heat transfer oils
Calculation of density and viscosity of heat transfer oils within the range
from 0 to 300 °C.
The calculated properties are approximate values. If you need very exact data
you should use measured values.
User database liquids
In this database you will find your own properties for liquids.
You can create several databases (as example aromatic hydrocarbons, heat
transfer oils) as Excel files. These files must saved in the program folder
"user-liquids" so the software can find the data. Please have a look in the
example files to arrange the data so the software can classify the properties of
the liquids. You can create or edit the database files with your Excel- or
OpenOffice-Software.
User database gases
In this database you will find your own properties for gases.
You can create several databases (as example hydrocarbons, nitrogen oxides)
as Excel files. These files must saved in the program folder "user-gases" so the
software can find the data. Please have a look in the example files to arrange
the data so the software can classify the properties of the gases. You can
create or edit the database files with your Excel- or OpenOffice-Software.