Risk based 3-dimensional and multifloor plant layout optimization for liquefied natural gas (LNG) liquefaction process

This paper presents a mathematical formulation for solving a 3-dimensional and multifloor plant layout problem with safety considerations. The presented model is formulated as a mixed integer non-linear programming (MINLP) model and quantifies risk by utilizing Dow’s fire and explosion index (Dow’s F&EI) system. The applicability of the model is demonstrated by an illustrative example regarding layout optimization for the C3MR liquefaction processes.

[1]  M. Thring World Energy Outlook , 1977 .

[2]  Ignacio E. Grossmann,et al.  An outer-approximation algorithm for a class of mixed-integer nonlinear programs , 1986, Math. Program..

[3]  A. R. Ciric,et al.  An MINLP Approach for Safe Process Plant Layout , 1996 .

[4]  J. P. Gupta,et al.  Application of DOW's fire and explosion index hazard classification guide to process plants in the developing countries , 1997 .

[5]  Ccps Guidelines for Chemical Process Quantitative Risk Analysis , 1999 .

[6]  Michael C. Georgiadis,et al.  A general mathematical programming approach for process plant layout , 1999 .

[7]  Lazaros G. Papageorgiou,et al.  Optimal multi-floor process plant layout , 2002 .

[8]  J. P. Gupta,et al.  Calculation of Fire and Explosion Index (F&EI) value for the Dow Guide taking credit for the loss control measures , 2003 .

[9]  Valerio Cozzani,et al.  The quantitative assessment of domino effect caused by overpressure. Part II. Case studies. , 2004, Journal of hazardous materials.

[10]  Valerio Cozzani,et al.  The quantitative assessment of domino effects caused by overpressure. Part I. Probit models. , 2004, Journal of hazardous materials.

[11]  Lazaros G. Papageorgiou,et al.  An MILP Approach to Safe Process Plant Layout , 2004 .

[12]  Mahmoud M. El-Halwagi,et al.  The integration of Dow's fire and explosion index (F&EI) into process design and optimization to achieve inherently safer design , 2007 .

[13]  G. Venkatarathnam Cryogenic mixed refrigerant processes , 2008 .

[14]  Lazaros G. Papageorgiou,et al.  Process plant layout using an improvement-type algorithm , 2009 .

[15]  Dongil Shin,et al.  Optimal multi-floor plant layout with consideration of safety distance based on mathematical programming and modified consequence analysis , 2011 .

[16]  Il Moon,et al.  Current status and future projections of LNG demand and supplies: A global prospective , 2011 .

[17]  Alessandro D. Trigilio,et al.  Modelling and Simulation of Natural Gas Liquefaction Process , 2012 .

[18]  Kyu-Yeul Lee,et al.  Optimal liquefaction process cycle considering simplicity and efficiency for LNG FPSO at FEED stage , 2014, Comput. Chem. Eng..