Tek-Tips is the largest IT community on the Internet today!
Members share and learn making Tek-Tips Forums the best source of peer-reviewed technical information on the Internet!
-
Congratulations cowski on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!
advantages of a flash ! ? 2
- Thread starter Dahb
- Start date
-
1
- #2
DickRussell
Chemical
First, natural gas is primarily methane, with lesser amounts of ethane, propane, nitrogen, etc. in it. There often is economic incentive to recover C3 and higher from natural gas, for use as LPG.
In general, separating components of differing volatilities is a matter of how different those volatilities are and of the degree of separation. With a very wide difference in boiling points (ex. methane from decane), the desired separation may well be done with a single stage (a flash drum). Since the remaining liquid exerts its vapor pressure in the vapor removed, closer volatilities means more impurity of the heavier material in the vapor, and multiple stages (a distillation column) may be needed. Cold temperatures result only from having to do the separations below the critical temperatures of the mixtures present at various points in the process. With very light materials, low temperatures are needed, and typically high pressure is needed to keep the temperatures from going too low, for various practical engineering reasons. The colder you go, the more difficult the refrigeration needed for condensing becomes.
Practical examples of low-temperature distillations are demethanizers and deethanizers in the hydrocarbon area and nitrogen-oxygen distillation in air separation. For a demethanizer, running at high pressure and a temperature of around -150 F or thereabouts, a refrigerant that much colder is needed (such as ethylene), pumping up to an intermediate level, perhaps needed for a downstream deethanizer, which may run at -40 F at the condenser, for which a propylene refrigerant will do. The intermediate level refrigerant in turn will pump up to cooling water. Refrigeration systems are a whole different subject.
In general, separating components of differing volatilities is a matter of how different those volatilities are and of the degree of separation. With a very wide difference in boiling points (ex. methane from decane), the desired separation may well be done with a single stage (a flash drum). Since the remaining liquid exerts its vapor pressure in the vapor removed, closer volatilities means more impurity of the heavier material in the vapor, and multiple stages (a distillation column) may be needed. Cold temperatures result only from having to do the separations below the critical temperatures of the mixtures present at various points in the process. With very light materials, low temperatures are needed, and typically high pressure is needed to keep the temperatures from going too low, for various practical engineering reasons. The colder you go, the more difficult the refrigeration needed for condensing becomes.
Practical examples of low-temperature distillations are demethanizers and deethanizers in the hydrocarbon area and nitrogen-oxygen distillation in air separation. For a demethanizer, running at high pressure and a temperature of around -150 F or thereabouts, a refrigerant that much colder is needed (such as ethylene), pumping up to an intermediate level, perhaps needed for a downstream deethanizer, which may run at -40 F at the condenser, for which a propylene refrigerant will do. The intermediate level refrigerant in turn will pump up to cooling water. Refrigeration systems are a whole different subject.
- Thread starter
- #3
hernanperut
Chemical
flash being use in azeotropic case when the usage of distillation column become uneconomic. thats relate to the composition, usually below 95% distillation column is preferable
- Thread starter
- #5
-
1
- #6
To use a flash you need a compresion ratio that can give you a good separation, while in distillation you dont need that but a temperature gradient, in any case you need energy to complete both, check your energy consumption for example you may have a high temperature current that can be helpful on distillation or your desired flow may have a very high preassure, that can be a criteria to choose wich method is best
- Status
Similar threads
- Locked
- Question
- Locked
- Question