الفهرس 
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Abstract
Natural gas dew point temperature is a vital quality parameter. The effective control of this specification is important if the natural gas integrity and quality are to be maintained. The present work focuses on improving the dew point temperature of natural gas processed in dew point control unit (DPCU) located in the Egyptian western desert and maximize condensate production from this unit. Improving hydrocarbon dew point temp. in the mentioned unit by using one of common refrigeration method (JT valve) to decrease natural gas temperature, this reduction in temperature causes heavy hydrocarbons to condense out of the gas phase to form liquids resulting in a residue gas with a lower dew point. Influence of the operational variables on outlet gas dew point and produced condensate were investigated. The simulation results estimated by designed case on HYSYS simulation program illustrated that feed gas inlet temperature, composition, Joule Thomson (JT) valve downstream, and upstream pressure and hot bypass flow rate have a great effect on the sales gas dew point as well as the condensate throughput. A field experiments were conducted to validate the simulation results. It is noticed that there is a good agreement between simulation and experimental results, considering the outlet gas dew point at different operating conditions. Lingo optimization software was used to find the plant optimum conditions. Two quadratic equations were developed based on regression analysis for calculating the dew point and plant condensate rate at any operational variables. The impact of replacing the existing JT valve by a turbo expander was studied. The simulation results indicate that the turbo expander is more effective in comparison with JT valve refrigeration system in decreasing the sales gas dew point and increasing the condensate production rate.