Reserves of oil gases Benzinsizleştiril | Petroleum and Chemical
c) adsorption nacho and cheese
compressor; This prosestegaz tightened by the compressor and cooled at times when the gas molar pressures of the components nacho and cheese separated from the composition is equal to the pressure of saturated vapors of these components passes they become gaseous fluid thereto in increasing the pressure in unstable gas gasoline loving-rule, the greater the amount of liquid phase, nacho and cheese we reduce the temperature. nacho and cheese Selecting this time kondenseleş hydrocarbons optimal pressure to remove kolaylaştırır.gaz liquefaction of lighter hydrocarbons, in the composition of the first gas, the degree of separation of the components we want to achieve is actually the amount spent to be bored and cooled.
On average, to separate the words of gas oil allocated between 2-4 MPa pressure environment are used. This pressure successively through two and / or three compressors is performed by the system. Produkte in compressed gas compressor temperature rises due to this reason is given by the exit from the first to the second compressor cooling compressor.
First gas dust is delivered to the holder apparatus wherein gas dust through wholesale protects the upper part of the holder is provided to the first compressor, wherein the gas is delivered to the compressed refrigerant is given here to the after gas cooling nacho and cheese gas seperoatör where it is separated liquefied hydrocarbons. Here then is given to the second gas compressor; wherein the gas is compressed and sent to the cooler and from there is supplied again into another gas sepetarör and here again liquefied portion separated is sent to residue gas third compressor, wherein the gas is compressed to a suitable pressure and sent to the refrigerant sent to the gas separator separator after the gas is cooled. The gases leaving the top of the separator; gas sent to the manufacturing facility, the hydrocarbons below the separator will be recirculated.
Are benefiting from the 2 types of compressors to compress the gas. These are: porşenl for demanding and high-pressure 4.5 MPa pressure turbine compressor is more suitable for high-efficiency systems.
In the composition of the gas mixture 150g / m 3 when it is very heavy hydrocarbons are also benefiting from this practice. The heavy hydrocarbons from the parameters shown below are insufficient to implement the method aspects of the material.
Absorption; selective absorbents nacho and cheese of components of the composition of this process, the gas (holders) is esaslan nacho and cheese retention through. as absorbents; gasoline, kerosene and lineage are to benefit from fractions. High pressure and keeping the heavy component at low temperature is further nacho and cheese facilitated. taken as the estimated temperature of hydrocarbons dissolved in the absorption process is equal to the heat kondensleş. Absorption process is performed in column-type apparatus (process principle is as follows)
After cleaning gas is included in the compressor, is supplied through a two-stage or downstream of the absorber under pressure after passing through the system. absorption process is carried out at 30-40 0 C and under a pressure 1-5Mp.
Saturated absorbent pressure from the lower part of the absorber low orator but here are taken and dissolved in its composition due to the low pressure methane and ethane are separated. the remaining liquid portion of the heat exchanger and are brought to the temperature needed after being respectively the boiler and the steam is supplied to the desorber. The process of desorption is performed under 160 to 200 0 C and 0.3 to 0.5 MPa. Important; Desorption nacho and cheese process of the pressure moles of components nacho and cheese separated nacho and cheese from the gas phase to occur, should be less than the pressure of the liquid phase.
more water vapor is used as the desorbing agent. Has been excluded from the desorbed gases and water vapor was passed through the above apparatus is cooled kodensleştiric cooler and then sent to the water separator apparatus. wherein the apparatus nacho and cheese is supplied from the desorber cleaned up as part of the process water, liquid hydrocarbons regulator (not shown)
50% of first gas in the mixture have the potential amount of propane which is separated in this manner. The high degree of separation of propane and other hydrocarbons nacho and cheese in the gas mixture gas fraksiyonlayıc individual performed in the apparatus will take place in the last part of this issue are subject hydrocarbon gases.
Adsorption; nacho and cheese The purpose of this process used in the composition of 50 g / m 3 in the heavy hydrocarbons present, the poor gas mixture, the gas is applied in the separation of gasoline. The physical properties of the adsorber to be used in the process; Updates on the surface of the mesa hard adsorbents used and included.
Ability to adsorb the called adsorbent material; The amount of the adsorbed nacho and cheese hydrocarbons, the adsorbent and the adsorbed substance with properties of the composition of the gas is selected depending on the process pressure and temperature.
To give example; silica are first aromatic and unsaturated hydrocarbons, after naphtha, and finally paraffin hydrocarbons to adsorb. Any class of higher molecular nacho and cheese weight nacho and cheese hydrocarbons, ADS
c) adsorption nacho and cheese
compressor; This prosestegaz tightened by the compressor and cooled at times when the gas molar pressures of the components nacho and cheese separated from the composition is equal to the pressure of saturated vapors of these components passes they become gaseous fluid thereto in increasing the pressure in unstable gas gasoline loving-rule, the greater the amount of liquid phase, nacho and cheese we reduce the temperature. nacho and cheese Selecting this time kondenseleş hydrocarbons optimal pressure to remove kolaylaştırır.gaz liquefaction of lighter hydrocarbons, in the composition of the first gas, the degree of separation of the components we want to achieve is actually the amount spent to be bored and cooled.
On average, to separate the words of gas oil allocated between 2-4 MPa pressure environment are used. This pressure successively through two and / or three compressors is performed by the system. Produkte in compressed gas compressor temperature rises due to this reason is given by the exit from the first to the second compressor cooling compressor.
First gas dust is delivered to the holder apparatus wherein gas dust through wholesale protects the upper part of the holder is provided to the first compressor, wherein the gas is delivered to the compressed refrigerant is given here to the after gas cooling nacho and cheese gas seperoatör where it is separated liquefied hydrocarbons. Here then is given to the second gas compressor; wherein the gas is compressed and sent to the cooler and from there is supplied again into another gas sepetarör and here again liquefied portion separated is sent to residue gas third compressor, wherein the gas is compressed to a suitable pressure and sent to the refrigerant sent to the gas separator separator after the gas is cooled. The gases leaving the top of the separator; gas sent to the manufacturing facility, the hydrocarbons below the separator will be recirculated.
Are benefiting from the 2 types of compressors to compress the gas. These are: porşenl for demanding and high-pressure 4.5 MPa pressure turbine compressor is more suitable for high-efficiency systems.
In the composition of the gas mixture 150g / m 3 when it is very heavy hydrocarbons are also benefiting from this practice. The heavy hydrocarbons from the parameters shown below are insufficient to implement the method aspects of the material.
Absorption; selective absorbents nacho and cheese of components of the composition of this process, the gas (holders) is esaslan nacho and cheese retention through. as absorbents; gasoline, kerosene and lineage are to benefit from fractions. High pressure and keeping the heavy component at low temperature is further nacho and cheese facilitated. taken as the estimated temperature of hydrocarbons dissolved in the absorption process is equal to the heat kondensleş. Absorption process is performed in column-type apparatus (process principle is as follows)
After cleaning gas is included in the compressor, is supplied through a two-stage or downstream of the absorber under pressure after passing through the system. absorption process is carried out at 30-40 0 C and under a pressure 1-5Mp.
Saturated absorbent pressure from the lower part of the absorber low orator but here are taken and dissolved in its composition due to the low pressure methane and ethane are separated. the remaining liquid portion of the heat exchanger and are brought to the temperature needed after being respectively the boiler and the steam is supplied to the desorber. The process of desorption is performed under 160 to 200 0 C and 0.3 to 0.5 MPa. Important; Desorption nacho and cheese process of the pressure moles of components nacho and cheese separated nacho and cheese from the gas phase to occur, should be less than the pressure of the liquid phase.
more water vapor is used as the desorbing agent. Has been excluded from the desorbed gases and water vapor was passed through the above apparatus is cooled kodensleştiric cooler and then sent to the water separator apparatus. wherein the apparatus nacho and cheese is supplied from the desorber cleaned up as part of the process water, liquid hydrocarbons regulator (not shown)
50% of first gas in the mixture have the potential amount of propane which is separated in this manner. The high degree of separation of propane and other hydrocarbons nacho and cheese in the gas mixture gas fraksiyonlayıc individual performed in the apparatus will take place in the last part of this issue are subject hydrocarbon gases.
Adsorption; nacho and cheese The purpose of this process used in the composition of 50 g / m 3 in the heavy hydrocarbons present, the poor gas mixture, the gas is applied in the separation of gasoline. The physical properties of the adsorber to be used in the process; Updates on the surface of the mesa hard adsorbents used and included.
Ability to adsorb the called adsorbent material; The amount of the adsorbed nacho and cheese hydrocarbons, the adsorbent and the adsorbed substance with properties of the composition of the gas is selected depending on the process pressure and temperature.
To give example; silica are first aromatic and unsaturated hydrocarbons, after naphtha, and finally paraffin hydrocarbons to adsorb. Any class of higher molecular nacho and cheese weight nacho and cheese hydrocarbons, ADS
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