ENERGY EFFICIENCY IMPROVEMENT FOR NATURAL GAS LIQUIDS DIRECT-SPLITTER-DIRECT SEQUENCE FRACTIONATION UNIT

Authors

  • Ahmad Nafais Rahimi Process Systems Engineering Centre (PROSPECT), Research Institute of Sustainability Environment (RISE), Faculty of Chemical and Energy Engineering (FCEE), Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
  • Mohd. Faris Mustafa Process Systems Engineering Centre (PROSPECT), Research Institute of Sustainability Environment (RISE), Faculty of Chemical and Energy Engineering (FCEE), Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
  • Muhammad Zakwan Zaine Process Systems Engineering Centre (PROSPECT), Research Institute of Sustainability Environment (RISE), Faculty of Chemical and Energy Engineering (FCEE), Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
  • Norazana Ibrahim UTM-MPRC Institute of Oil & Gas, Faculty of Chemical and Energy Engineering (FCEE), Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
  • Kamarul Asri Ibrahim Process Systems Engineering Centre (PROSPECT), Research Institute of Sustainability Environment (RISE), Faculty of Chemical and Energy Engineering (FCEE), Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
  • Nooryusmiza Yusoff School of Engineering and Physical Sciences, Heriot-Watt University Malaysia, No 1 Jalan Venna P5/2, Precint 5, 62200 Putrajaya, Malaysia
  • Eid M. Al-Mutairi Department of Chemical Engineering, King Fahd University of Petroleum & Minerals, Dhahran 31261, Saudi Arabia
  • Mohd. Kamaruddin Abd. Hamid Process Systems Engineering Centre (PROSPECT), Research Institute of Sustainability Environment (RISE), Faculty of Chemical and Energy Engineering (FCEE), Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia

DOI:

https://doi.org/10.11113/jt.v78.9236

Keywords:

Energy Efficient, Distillation Columns Sequence, Driving Force, Natural Gas Liquid

Abstract

The objective of this paper is to present the study and analysis of the energy saving improvement for the NGLs Direct-Splitter-Direct fractionation sequence plant by using driving force method. To perform the study and analysis, the energy efficient distillation columns (EEDCs) methodology is developed. Basically, the methodology consists of four hierarchical steps; Step 1: Existing Sequence Energy Analysis, Step 2: Optimal Sequence Determination, Step 3: Optimal Sequence Energy Analysis, and Step 4: Energy Comparison. The capability of this methodology is tested in designing an optimal energy efficient direct-splitter-direct sequence of NGLs fractionation unit. The results show that the maximum of 10.62 % energy reduction was able to achieve by changing the sequence suggested by the driving force method. It can be concluded that, the sequence determined by the driving force method is able to reduce energy used for a NGLs fractionation. All of this findings show that the methodology is able to design energy efficient for NGLs fractionation sequence in an easy, practical and systematic manner.

References

Hernandez, S., Gabrielsegoviahernandez, J. and Ricoramirez, V. 2006. Thermo Dynamically Equivalent Distillation Schemes To The Petlyuk Column For Ternary Mixtures. Energy. 31(12): 2176-2183.

U. S. Dept. of Energy. Office of Energy Efficiency and Renewable Energy. Distillation column modeling tools. Department of Energy (DOE). Washington DC. http://www1.eere.energy.gov/manufacturing/industries_technologies/chemicals/pdfs/distillation.pdf.

Lucia, A. and McCallum, B. R. 2010. Energy Targeting And Minimum Energy Distillation Column Sequences. Computers and Chemical Engineering. 34(6): 931-942.

Grossmann, E. I., Caballero, A. J. and Yeomans, H. 2000. Advances in Mathematical Programming for Automated Design, Integration and Operation of Chemical Processes. Latin American Applied Research. 30(4): 263-284.

Floquet, P., Pibouleau, L. and Domenech, S. 1988. Mathematical Programming Tools For Chemical Engineering Process Design Synthesis. Chem. Eng. Process. 23(1): 99-113

Floquet, P., Pibouleau, L. and Domenech, S. 1994. Separation Sequence Synthesis: How To Use Simulated Annealing Procedure. Computers and Chemical Engineering. 18 (11/12): 1141-1148.

Gert-Jan, A. F. and Liu, Y. A. 1994. Heuristic Synthesis And Shortcut Design Of Separation Processes Using Residue Cuve Maps: A Review. Ind. Eng. Chem. Res. 33(11): 2505-2522.

Westerberg, A. W. 1985. The Synthesis Of Distillation-Based Separation Systems. Computers and Chemical Engineering. 9(5): 421-429.

Floudas, C. A. 1995. Nonlinear and Mixed-Integer Optimization: Fundamentals and Applications. USA: Oxford University Press

Mustafa, M. F., Abdul Samad, N. A. F., Ibrahim, K. A., Hamid, M. K. A. 2014. Methodology Development For Designing Energy Efficient Distillation Column Systems. Energy Procedia. 61: 2550-2553.

Seader, J. D. and Westerberg, A. W. 1977. A Combined For Synthesis Heuristic And Evolutionary Strategy Of Simple Separation Sequences. AIChE Journal. 23(6): 951-954.

Stephanopoulos, G. and Westerberg, A. W. 1976. Studies In Process Synthesis II Evolutionary Synthesis Of Optimal Process Flowsheets. Chem. Eng. Sci. 31(3): 195-204.

Nadgir, V. M. and Liu, Y. A. 1983. Studies In Chemical Process Design And Synthesis Part V: A Simple Heuristic Method For Systematic Synthesis Of Initial Sequences For Multicomponent Separations. AIChE Journal. 29(6): 926-934.

Rudd, D. F., Powers, G. J., and Siirola, J. J. 1973. Process Synthesis. New Jersey: Prentice-Hall.

Tedder, D. W. & Rudd, F. D. 1978. Parametric Studies In Industrial Distillation: Part I Design Comparisons. AIChE Journal. 24(2): 303-315.

Seider, W. D., Seader, J. D. and Lewin, D. R. 2004. Product and Process Design Principles: Synthesis, Analysis, and Evaluation. New York: Wiley

Modi, A. & Westerberg, A. 1992. Distillation Column Sequencing Using Marginal Price. Ind. Eng. Chem. Res. 31(3): 839-848.

Floudas, C. A. 1987. Separation Synthesis Of Multicomponent Feed Streams Into Multicomponent Product Streams. AIChE Journal. 33(4): 540-550.

Wehe, R. R. & Westerberg, A. W. 1990. A Bounding Procedure For The Minimum Number Of Columns In Nonsharp Distillation Sequences. Chem. Eng. Sci. 45(1): 1-11.

Sobocan, G. and Glavic, P. A. 2012. A Simple Method For Systematic Synthesis Of Thermally Integrated Distillation Sequences. Chemical Engineering Journal. 89(1-3): 155-172.

Bek-Pedersen, E. and Gani, R. 2004. Design And Synthesis Of Distillation Systems Using A Driving Force Based Approach. Chemical Engineering and Processing. 43(3): 251-262.

Kemp, I. C. 2007. Pinch Analysis and Process Integration. A User Guide on Process Integration for the Efficient Use of Energy. Amsterdam: Elsevier.

Wang, J. L. and Mansoori, G. A. 1994. A Revision Of The Distillation Theory (Part I). Scientia Ir. 1(3): 267-287.

Mustafa, M. F., Abdul Samad, N. A. F., Ibrahim, N., Ibrahim, K. A. and Hamid, M. K. A. 2015. Energy Efficient Distillation Columns Design For Retrofit Ngls Fractionation Process. Advanced Materials Research. 1113: 667-673

Long, N. V. D. & Lee, M. 2011. Improved Energy Efficiency In Debottlenecking Using A Fully Thermally Coupled Distillation Column. Asia-Pac. J. Chem. Eng. 6(3): 338-348.

Downloads

Published

2016-06-23

How to Cite

ENERGY EFFICIENCY IMPROVEMENT FOR NATURAL GAS LIQUIDS DIRECT-SPLITTER-DIRECT SEQUENCE FRACTIONATION UNIT. (2016). Jurnal Teknologi, 78(6-12). https://doi.org/10.11113/jt.v78.9236