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Journal of Petroleum and Gas Exploration Research (ISSN 2276-6510) Vol. 3(3) pp. 31-39, July, 2013 Available online http://www.interesjournals.org/JPGER Copyright © 2013 International Research Journals
Review
Dynamic modelling and simulation of crude fractionation column with three side strippers us Aspen HYSYS Dynamics: A best practice for cru distillation column dynamic modelling 1
R Parthiban, 2N Nagarajan, 3V Mahendra Kumaran, 4*D Senthil Kumar 1
Head of the Department, Chemical Engineering, SVCE, Sriperumpudur, India 2 Head of the Department, Process, Petrofac, Chennai, India 3 Principal Process Engineer, Petrofac, Chennai, India 4 M. Tech - Scholar, Chemical Engineering, SVCE, Chennai, India Accepted May 22, 2013
Steady state and Dynamic simulations play a vital role in most of the Refineries and Petroc industries to evaluate and optimize key process variables. Apart from operation, simulatio in design engineering in many ways. Simulation allows studying the transient beha Read Free Foron 30this Days Sign up to vote title You're Reading Preview complex processes without the need of real plant aoperating information or even withou Useful Not useful plant. In this study, dynamic simulation is applied to atmospheric distillation unit (AD Cancel anytime. full access with a free trial.processes characterised by Crude oil refining processUnlock is one of the complex Special offerrefinery. for students: Only $4.99/month. interactions and high level of non-linearity. This paper describes the best prac
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32 J. Pet. Gas Explor. Res.
Table 1. Selection of Property Method
Type of System
Recommended Property Method
TEG Dehydration Sour Water Cryogenic Gas Processing Air Separation Atmospheric Crude Towers Vacuum Towers Ethylene Towers High H2 Systems Reservoir Systems Steam Systems Hydrate Inhibition Chemical Systems HF Alkylation TEG Dehydration with Aromatics HC Systems where H2O solubility in HC is important Systems with select gases and light HC
PR Sour PR PR, PRSV PR, PRSV PR, PR Options, GS PR, PR Options, GS (<10mm Hg), Braun K10, Lee Kesler Plocker PR, ZJ or GS PR, PR Options Steam Package, CS or GS PR Activity Models, PRSV PRSV, NRTL PR Kabadi Danner MBWR
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Method Temp ( C) Pressure (kPa) PR -271 100,000
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Par
Figure 1. TBP Curve for Crude Assay
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assay.
characterize petroleum assay.
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34 J. Pet. Gas Explor. Res.
Figure 2. Product Cut Distribution for Crude Assay
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Part
Table 6. Degrees of Freedom specifications
Specifications Off Gas Rate (TPH) LPG Rate (TPH) Kerosene Rate (TPH) LGO Rate (TPH) HGO Rate (TPH) Pump Around-1 Rate (TPH) Pump Around-2 Rate (TPH) Pump Around-3 Rate (TPH) o Pump Around-1 ∆T ( C) o Pump Around-2 ∆T ( C) o Pump Around-3 ∆T ( C) o Gap Cut Point ( C) Kero SS Reb Duty (MJ/Hr.)
5 325 270 110 20 700 700 700 60 60 60 25 60,000
strippers, crude semester distillation columns are characterized etc.) A resistance equation Master your with Scribdby (vessels, operat Read Free Foron 30 Days Signdrop up tobased vote this multiple interactions and high level of non-linearity due to on atitle resistance equa You're Reading apressure Preview complexity of process. compressors, valves, etc.). & TheTheNew York Times Useful Not useful total degrees of freedom to converge a typical In the Process Flow Diagram (PFD), there Cancel anytime.
Unlock full access with a free trial. Special offer forcolumn students:with Onlythree $4.99/month. crude side stripper are 13. Closest least one resistance operation in between assumptions of thirteen relevant variables have been pressure nodes. Else, the solver may ass
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36 J. Pet. Gas Explor. Res. Table 7. Recommended Vessel sizing
Service
Residence Time
Liquid phase hold-ups Vapour phase hold-ups
10 minutes 2 minutes
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Table 8. Recommended Controller Tuning Values
System Flow Level Pressure Temperature
Kc 0.1 2 2 1
(mins.) 0.2 10 2 20
(mins.) 0 0 0 0
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38 J. Pet. Gas Explor. Res.
Figure7. Boiling Point Curves for Light Gas Oil
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