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Depriester chart kpa and celsius
Depriester chart kpa and celsius











33 3.2.2 Modelling and Simulation of Petlyuk Columns. 33 3.2.1 Minimum Energy Mountain Diagram.

depriester chart kpa and celsius

Date and signature:ĪCKNOWLEDGEMENT.iv ABSTRACT. However, all the configurations are found to be highly sensitive to both raw materials as well as product prices. Conclusions and recommendations: Out of the six alternative cases studied, three conventional and three with Petlyuk columns, the Petlyuk column producing LPG and natural gasoline, is found out to be economically most profitable. In order to have an economic process, instead of using refrigerant it is suggested to use sea water, at 10oC for condenser. Thus, the steam used for reboiler of the column is considered to be generated as part of steam generation for the whole plant. The plant will be built in Norway as a part of a gas processing plant. The process is studied using conventional columns and also Petlyuk columns as alternative to the conventional ones. Written by: Eldar Khabibullin, Feby Febrianti, Juejing Sheng and Sulalit Bandyopadhyay Supervisor: Sigurd Skogestad Co-Supervisors: Mehdi Panahi and Maryam GhadrdanĮXTRACT OF WORK AND CONCLUSIONS Postulations and dimension of work: The LPG recovery plant operates on Natural Gas Liquids (NGL), entering from two sources, with a total flowrate of 33 tonnes/hour and produces Liquified Petroleum Gas (LPG) along with Natural Gasoline as the primary products. Title: Process Design and Economic Investigation of LPG Production from Natural Gas Liquids (NGL) Keyword (3-4): LPG Recovery, Petlyuk Column, Economic Evaluation Time of work: August 26th, 2010 ­ November 18th, 2010 Number of pages: 99 Main report: 74 Appendix : 25 NTNU Norwegian University of Science and Technologyįaculty of Natural Sciences and Technology Department of Chemical Engineering

depriester chart kpa and celsius

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Depriester chart kpa and celsius