An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature

Khalid Farhod Chasib; Srikanth Karthik P.

doi:doi:10.11648/j.ogce.20170505.13

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An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature

Khalid Farhod Chasib, Srikanth Karthik P.

Published in International Journal of Oil, Gas and Coal Engineering (Volume 5, Issue 5)

Received: 31 October 2016 Accepted: 22 December 2016 Published: 24 October 2017

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Abstract

For the reliable design of crude oil and residua fractionators and fired heaters, accurate calculation method for ASTM Distillation curves and ASTM distillation temperature at the required volume percentage distilled is necessary. The present work deals with fitting literature data of ASTM Distillation curves and obtain a new correlation suitable to use in modeling when optimizing the refining processes, such as distillation, FCC, catalytic reforming, hydrotreating, etc. The results showed that the values predicted by the new correlation are in very close agreement with literature data and the range of mean overall deviation (%MOD) is (0.305-0.585). Also a shortcut correlation is presented to calculate the ASTM distillation temperature at the required volume percentage distilled. Based on temperatures obtained we can have an estimate of the heating costs involved to perform distillation and temperature at which different cuts are obtained.

Published in	International Journal of Oil, Gas and Coal Engineering (Volume 5, Issue 5)
DOI	10.11648/j.ogce.20170505.13
Page(s)	80-89
Creative Commons	This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.
Copyright	Copyright © The Author(s), 2017. Published by Science Publishing Group

Keywords

Distillation Curves, ASTM, Refining Processes

References

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[4]	L. A. Alcazar, J. Ancheyta,(2007), Sensitivity analysis based methodology to estimate the best set of parameters for heterogeneous kinetic models, Chemical Engineering Journal 12885–93.
[5]	S. Sanchez, J. Ancheyta, W. C. McCaffrey,(2007), Comparison of Probability Distribution Functions for Fitting Distillation Curves of Petroleum, Energy & Fuels, 21, 2955-2963.
[6]	Batistella, C. B., (1999), PHD Thesis (in Portuguese), UNICAMP, SP, Brazil.
[7]	Batistella, C. B. E Maciel, M. R. W., (1998), Comput. Chem. Eng., v. 22, S53-S60.
[8]	Burrows, G, (1960), Molecular Distillation. Oxf. Univ. Press (Oxford).
[9]	Boduszynski, M. M E Altgelt, K. H., (1994), Composition end Analysis of Heavy Petroleum Fractions. Marcel Dekker, Inc., NY.
[10]	Batistella, C. B., Sbaite, P., Wolf Maciel, M. R., Maciel Filho, R., Winter, A., Gomes, A., Medina, L., Kunert, R, (2005), Heavy Petroleum Fractions Characterization: A New Approach Through Molecular Distillation, 2^nd Mercosul Congress on Chemical Engineering & 4th Mercosul Congress on Process Systems Engineering (ENPROMER 2005), Costa Verde – RJ, Brazil.
[11]	Winter, A., Batistella, C. B., Wolf Maciel, M. R., Maciel Filho, R., Lopes, M. S. Medina, L. C., A True Boiling Point Curve Through Molecular Distillation Using FRAMOL Correlation, Internet resources available at (http://www.nt.ntnu.no/users/skoge/prost/proceedings/icheap8-pres07/icheap8webpapers/109%20Winter.pdf)
[12]	Randy B., Ian B., (2006), Sensitivity of Oil Fate Model Predictions to Oil Property Inputs, Can. J Chem. Engng, 83, 3.
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[16]	Jones D. S. D. and Pujado P. R., (2006). Handbook of Petroleum Processing, Springer, Netherlands.
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APA Style

Khalid Farhod Chasib, Srikanth Karthik P. (2017). An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature. International Journal of Oil, Gas and Coal Engineering, 5(5), 80-89. https://doi.org/10.11648/j.ogce.20170505.13

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ACS Style

Khalid Farhod Chasib; Srikanth Karthik P. An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature. Int. J. Oil Gas Coal Eng. 2017, 5(5), 80-89. doi: 10.11648/j.ogce.20170505.13

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AMA Style

Khalid Farhod Chasib, Srikanth Karthik P. An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature. Int J Oil Gas Coal Eng. 2017;5(5):80-89. doi: 10.11648/j.ogce.20170505.13

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@article{10.11648/j.ogce.20170505.13,
  author = {Khalid Farhod Chasib and Srikanth Karthik P.},
  title = {An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature},
  journal = {International Journal of Oil, Gas and Coal Engineering},
  volume = {5},
  number = {5},
  pages = {80-89},
  doi = {10.11648/j.ogce.20170505.13},
  url = {https://doi.org/10.11648/j.ogce.20170505.13},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ogce.20170505.13},
  abstract = {For the reliable design of crude oil and residua fractionators and fired heaters, accurate calculation method for ASTM Distillation curves and ASTM distillation temperature at the required volume percentage distilled is necessary. The present work deals with fitting literature data of ASTM Distillation curves and obtain a new correlation suitable to use in modeling when optimizing the refining processes, such as distillation, FCC, catalytic reforming, hydrotreating, etc. The results showed that the values predicted by the new correlation are in very close agreement with literature data and the range of mean overall deviation (%MOD) is (0.305-0.585). Also a shortcut correlation is presented to calculate the ASTM distillation temperature at the required volume percentage distilled. Based on temperatures obtained we can have an estimate of the heating costs involved to perform distillation and temperature at which different cuts are obtained.},
 year = {2017}
}

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TY  - JOUR
T1  - An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature
AU  - Khalid Farhod Chasib
AU  - Srikanth Karthik P.
Y1  - 2017/10/24
PY  - 2017
N1  - https://doi.org/10.11648/j.ogce.20170505.13
DO  - 10.11648/j.ogce.20170505.13
T2  - International Journal of Oil, Gas and Coal Engineering
JF  - International Journal of Oil, Gas and Coal Engineering
JO  - International Journal of Oil, Gas and Coal Engineering
SP  - 80
EP  - 89
PB  - Science Publishing Group
SN  - 2376-7677
UR  - https://doi.org/10.11648/j.ogce.20170505.13
AB  - For the reliable design of crude oil and residua fractionators and fired heaters, accurate calculation method for ASTM Distillation curves and ASTM distillation temperature at the required volume percentage distilled is necessary. The present work deals with fitting literature data of ASTM Distillation curves and obtain a new correlation suitable to use in modeling when optimizing the refining processes, such as distillation, FCC, catalytic reforming, hydrotreating, etc. The results showed that the values predicted by the new correlation are in very close agreement with literature data and the range of mean overall deviation (%MOD) is (0.305-0.585). Also a shortcut correlation is presented to calculate the ASTM distillation temperature at the required volume percentage distilled. Based on temperatures obtained we can have an estimate of the heating costs involved to perform distillation and temperature at which different cuts are obtained.
VL  - 5
IS  - 5
ER  -

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Author Information

Khalid Farhod Chasib

Head of the Petroleum & Gas Engineering Department, Collage of Engineering, University of Thi Qar, Thi Qar, Iraq
Srikanth Karthik P.

Visakh Refinery, Hindustan Petroleum Corporation Limited, Visakhapatnam, India

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APA Style

Khalid Farhod Chasib, Srikanth Karthik P. (2017). An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature. International Journal of Oil, Gas and Coal Engineering, 5(5), 80-89. https://doi.org/10.11648/j.ogce.20170505.13

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ACS Style

Khalid Farhod Chasib; Srikanth Karthik P. An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature. Int. J. Oil Gas Coal Eng. 2017, 5(5), 80-89. doi: 10.11648/j.ogce.20170505.13

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AMA Style

Khalid Farhod Chasib, Srikanth Karthik P. An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature. Int J Oil Gas Coal Eng. 2017;5(5):80-89. doi: 10.11648/j.ogce.20170505.13

Copy | Download

@article{10.11648/j.ogce.20170505.13,
  author = {Khalid Farhod Chasib and Srikanth Karthik P.},
  title = {An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature},
  journal = {International Journal of Oil, Gas and Coal Engineering},
  volume = {5},
  number = {5},
  pages = {80-89},
  doi = {10.11648/j.ogce.20170505.13},
  url = {https://doi.org/10.11648/j.ogce.20170505.13},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ogce.20170505.13},
  abstract = {For the reliable design of crude oil and residua fractionators and fired heaters, accurate calculation method for ASTM Distillation curves and ASTM distillation temperature at the required volume percentage distilled is necessary. The present work deals with fitting literature data of ASTM Distillation curves and obtain a new correlation suitable to use in modeling when optimizing the refining processes, such as distillation, FCC, catalytic reforming, hydrotreating, etc. The results showed that the values predicted by the new correlation are in very close agreement with literature data and the range of mean overall deviation (%MOD) is (0.305-0.585). Also a shortcut correlation is presented to calculate the ASTM distillation temperature at the required volume percentage distilled. Based on temperatures obtained we can have an estimate of the heating costs involved to perform distillation and temperature at which different cuts are obtained.},
 year = {2017}
}

Copy | Download

TY  - JOUR
T1  - An Investigation on the Feasibility of Simulating the Distillation Curves and ASTM Distillation Temperature
AU  - Khalid Farhod Chasib
AU  - Srikanth Karthik P.
Y1  - 2017/10/24
PY  - 2017
N1  - https://doi.org/10.11648/j.ogce.20170505.13
DO  - 10.11648/j.ogce.20170505.13
T2  - International Journal of Oil, Gas and Coal Engineering
JF  - International Journal of Oil, Gas and Coal Engineering
JO  - International Journal of Oil, Gas and Coal Engineering
SP  - 80
EP  - 89
PB  - Science Publishing Group
SN  - 2376-7677
UR  - https://doi.org/10.11648/j.ogce.20170505.13
AB  - For the reliable design of crude oil and residua fractionators and fired heaters, accurate calculation method for ASTM Distillation curves and ASTM distillation temperature at the required volume percentage distilled is necessary. The present work deals with fitting literature data of ASTM Distillation curves and obtain a new correlation suitable to use in modeling when optimizing the refining processes, such as distillation, FCC, catalytic reforming, hydrotreating, etc. The results showed that the values predicted by the new correlation are in very close agreement with literature data and the range of mean overall deviation (%MOD) is (0.305-0.585). Also a shortcut correlation is presented to calculate the ASTM distillation temperature at the required volume percentage distilled. Based on temperatures obtained we can have an estimate of the heating costs involved to perform distillation and temperature at which different cuts are obtained.
VL  - 5
IS  - 5
ER  -

Copy | Download