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PREDICTING THE PRODUCTS OF CRUDE OIL DISTILLATION COLUMNS A thesis submitted to the University of Manchester for the degree of Master of Philosophy.


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The aim of this research was to simulate a high-pressure (HP) separator in order to investigate the effect of changing separator operating conditions on product properties. In this study, the results obtained using the CHEMCAD simulation software package were compared with those obtained using the UniSim software package. The simulation results were comparable with industrial data.

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At its core, manufacturing simulation is an inexpensive, risk-free way to test anything from simple revisions to complete redesigns, always with the purpose of meeting production goals at the lowest possible cost. Simulation also provides a way to test and implement principles of Lean manufacturing and Six Sigma. And unlike spreadsheet-based analysis and forecasting, manufacturing simulation.

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Peng-Robinson 1979 (PR-1979) was used as the EOS model in the HYSYS, PROSPER and SENSOR simulators. A check was A check was made on the consistency of all PVT calculations.


One way of classifying distillation column type is to look at how they are operated. Thus we have: batch and: continuous columns. Batch Columns: In batch operation, the feed to the column is introduced batch-wise. That is, the column is charged with a 'batch' and then the distillation process is carried out. When the desired task is achieved, a next batch of feed is introduced. Continuous.

The aim of this work is to optimize the conceptual design of an amine-based carbon dioxide (CO2) separation process for Enhanced Oil Recovery (EOR). A systematic approach is applied to predict the economic profitability of the system while reducing the environmental impacts. Firstly, we model the process with UniSim and determine the governing degrees of freedom (DoF) through a sensitivity.


Structured packing consists of arrangements of corrugated steel internals, over which the glycol flows downwards as a thin film. Elements of structured packing are illustrated in Fig. 4.The gas flows upward through the structured packing and is in intimate contact with the large surface area of the glycol that flows downward as a film on the packing.

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Buku panduan untuk program sarjana Teknik UI. 1 2 3 4 The Committee Chair Advisory Committee Editor-in-chief Editor Cover Design: Dean of Engineering Prof. Dr. Ir.

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Academic Guidebook FT UI - Tentang FTUI 1 2 3 4 The Committee Chair: Dean of Engineering Prof. Dr. Ir. Dedi Priadi, DEA Advisory Committee: Dr. Ir. M. Asvial, M.Eng.

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Fractional distillation works because the different liquids have different boiling points. When the mixture is heated: vapours rise through a column which is hot at the bottom, and cold at the top.

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