Hydrocarbon dew point temperature Calculator
Hydrocarbon dew point temperature / s, compositions, K values, liquid and vapour compressibility factor values, liquid and vapour densities and liquid and vapour molecular weight at desired pressure.
Equilibrium temperature, compositions, K values and compressibility factor values at pressure values throughout the hydrocarbon dew point curve at increments of 0.4 bars.
Phase envelope temperature at increments of 0.4 bars throughout the phase envelope and phase envelope curve.
Hydrocarbon dew point temperature is the temperature at which first drop of liquid is formed from a hydrocarbon mixture originally in vapor form at a given pressure. At a given pressure, a pure hydrocarbon converts from liquid to vapor at a specified temperature. However, a hydrocarbon mixture converts from liquid to vapor within a range of temperatures at a given pressure. A hydrocarbon mixture starts converting from vapor to liquid state at hydrocarbon dew point temperature at a constant pressure. Hydrocarbon dew point temperature is also known as final boiling point or final boiling temperature. At low pressures, only one hydrocarbon dew point temperature exists for a hydrocarbon mixture. However at high pressures two hydrocarbon dew point temperature values can exist. For hydrocarbon mixtures with components with wide difference in volatilities three hydrocarbon dew point temperature values can also exist for some pressure values below cricondenbar pressure.
Hydrocarbon dew point temperature values are used as design parameters for distillation columns. Hydrocarbon dew point temperature values are also used to design compressors and gas pipelines. Hydrocarbon dew point temperature values are used to calculate superheat temperature values which are specified in natural gas contracts. The superheat temperature is the minimum temperature at which natural gas is to be supplied to gas turbines so as to avoid condensation of natural gas on turbine blades avoid any damage to natural gas turbines. Apart from these, hydrocarbon dew point temperature values have got extensive usage in all kinds of engineering calculations involving hydrocarbons.
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Calculation cost (without Binary Interaction Parameters) : USD 75
Calculation cost (with constant or user defined BIPs) : USD 100