Siting Optimization of Facility and Unit Relocation with the Simultaneous Consideration of Economic and Safety Issues

A general optimization model is proposed to determine the optimal plant layout with the simultaneous consideration of economic and safety aspects. An important characteristic of the proposed optimization model is that it allows the relocation of some of the existing units to reduce the risks associated with current locations. The formulation also allows the addition of new units. A multiobjective mixed-integer linear programming model (MO-MILP) is developed to determine the optimal location of new and existing units while accounting for cost and risk. The proposed model is analyzed through a case study for a hexane distillation process showing the advantages of considering the possibility of relocating units originally installed following exclusively heuristic approaches and economic criteria.

[1]  J. Vrijling,et al.  An overview of quantitative risk measures for loss of life and economic damage. , 2003, Journal of hazardous materials.

[2]  Michael C. Georgiadis,et al.  Layout of process plants: A novel approach , 1997 .

[3]  Matthew J. Realff,et al.  Geographic and process information for chemical plant layout problems , 1999 .

[4]  Lazaros G. Papageorgiou,et al.  Continuous-Domain Mathematical Models for Optimal Process Plant Layout , 1998 .

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

[6]  G. Reklaitis,et al.  Chemical plant layout via graph partitioning-1. Single level , 1994 .

[7]  Dongil Shin,et al.  Risk Index Approach for the Optimal Layout of Chemical Processes Minimizing Risk to Humans , 2013 .

[8]  R. Raman,et al.  Modelling and computational techniques for logic based integer programming , 1994 .

[9]  Roy E Sanders Designs that lacked inherent safety: case histories. , 2003, Journal of hazardous materials.

[10]  Elwood S. Buffa,et al.  A Heuristic Algorithm and Simulation Approach to Relative Location of Facilities , 1963 .

[11]  Ken Paterson,et al.  The design of BP ETAP platform against gas explosions , 1999 .

[12]  Wenguo Weng,et al.  An integrated quantitative risk analysis method for natural gas pipeline network , 2010 .

[13]  Carl D. Laird,et al.  A new approach for facility siting using mapping risks on a plant grid area and optimization , 2010 .

[14]  Mahmoud M. El-Halwagi,et al.  Multiobjective optimization of biorefineries with economic and safety objectives , 2013 .

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

[16]  Gintaras V. Reklaitis,et al.  Chemical plant layout via graph partitioning—II. Multiple levels , 1996 .

[17]  M. Sam Mannan,et al.  An approach to solve the facility layout problem based on the worst-case scenario , 2010, Journal of Loss Prevention in the Process Industries.

[18]  Lazaros G. Papageorgiou,et al.  A Construction-Based Approach to Process Plant Layout Using Mixed-Integer Optimization , 2007 .

[19]  Mahmoud M. El-Halwagi,et al.  On the environmental, economic and safety optimization of distributed treatment systems for industrial effluents discharged to watersheds , 2013 .

[20]  Dedy Ng,et al.  New Approach To Optimizing the Facility Siting and Layout for Fire and Explosion Scenarios , 2011 .

[21]  M. Sam Mannan,et al.  Optimal facility layout under toxic release in process facilities: A stochastic approach , 2010, Comput. Chem. Eng..