The parameters for the proper operation of each one of the process stages (compression, cooling, and separation) in an existing gas processing plant which processes 1.5 million standard cubic feet per day (MMSCFD) were determined. The gas plant was simulated using the Aspen HYSYS® V7.3 software with the current operational plant conditions and the measured properties of the fluids (gas chromatography for input gas, fuel gas, and LPG). Subsequently, unidimensional searches were performed via sensitivity analyses of the key stages of the process to obtain suitable parameters for improving naphtha production. This resulted in a maximum naphtha recovery rate of 99.13% (which is an improvement over the current recovery rate of 82.79%) and an inc...
AbstractAn approach to modeling the isomerization process implemented in the technological scheme wi...
Computer aided process design is improving with newer and newer tools. One of such tools is the auto...
Simulation and design of a delayed coking plant for the treatment of oil waste with 6.5° API coming...
The parameters for the proper operation of each one of the process stages (compression, cooling, and...
This study estimates the parameters for the proper operation of each one of the process stages (comp...
Energy optimization is of vital importance especially in oil, gas and petrochemical industries. Dist...
The naphtha recovery unit (NRU) is an integral part of the processes used in the oil sands industry ...
Natural gas (NG) is naturally generated gas mixture lying under the earth and collected from gas wel...
The objective of this work is to make a simulation to be possible to reproduce and to optimize the o...
The operation of a gas processing plant with a tight profit margin and rigid contractual constraints...
NoIn this paper, a model of catalytic naphtha reforming process of commercial catalytic reforming un...
A model of a chemical process plant with recycle streams was simulated on a digital computer using t...
Fluid Catalytic Cracking Unit is the pump house of any refinery. Distillation is the initial step in...
A coupled furnace/reactor simulation was conducted to determine product yields and coking rates for ...
An approach to simulation of hydrocarbons refining processes catalytic reactors. The kinetic and the...
AbstractAn approach to modeling the isomerization process implemented in the technological scheme wi...
Computer aided process design is improving with newer and newer tools. One of such tools is the auto...
Simulation and design of a delayed coking plant for the treatment of oil waste with 6.5° API coming...
The parameters for the proper operation of each one of the process stages (compression, cooling, and...
This study estimates the parameters for the proper operation of each one of the process stages (comp...
Energy optimization is of vital importance especially in oil, gas and petrochemical industries. Dist...
The naphtha recovery unit (NRU) is an integral part of the processes used in the oil sands industry ...
Natural gas (NG) is naturally generated gas mixture lying under the earth and collected from gas wel...
The objective of this work is to make a simulation to be possible to reproduce and to optimize the o...
The operation of a gas processing plant with a tight profit margin and rigid contractual constraints...
NoIn this paper, a model of catalytic naphtha reforming process of commercial catalytic reforming un...
A model of a chemical process plant with recycle streams was simulated on a digital computer using t...
Fluid Catalytic Cracking Unit is the pump house of any refinery. Distillation is the initial step in...
A coupled furnace/reactor simulation was conducted to determine product yields and coking rates for ...
An approach to simulation of hydrocarbons refining processes catalytic reactors. The kinetic and the...
AbstractAn approach to modeling the isomerization process implemented in the technological scheme wi...
Computer aided process design is improving with newer and newer tools. One of such tools is the auto...
Simulation and design of a delayed coking plant for the treatment of oil waste with 6.5° API coming...