Using process stream index (PSI) to assess inherent safety level during preliminary design stage

In the current practice, safety assessment is conducted once the process design has been completed. At this stage of design, the freedom to change the conceptual design is very limited and whatever strategies to be implemented will only control the hazard. This paper reports on the development of inherent safety index known as a process stream index (PSI) for inherent safety level assessment at preliminary design stage from the perspective of an explosion. The aim for PSI is to calculate, compare and prioritize the level of inherent safety of process streams during simulation work that influences the explosion. By prioritizing the streams based on the potential for the explosion, the design engineers can easily identify the critical streams to be considered for improvement in order to avoid or minimize explosion hazards. An enhancement technique to reflect the contribution of the individual components in the mixture is introduced, which provide significant contribution to the ranking of inherent safety level of process streams. The assessment of inherent safety level using PSI is demonstrated by case studies of HYSYS simulation for Acrylic Acid Plant and Natural Gas Liquid (NGL) plant.

[1]  Azmi Mohd Shariff,et al.  Toxic release consequence analysis tool (TORCAT) for inherently safer design plant. , 2010, Journal of hazardous materials.

[2]  Azmi Mohd Shariff,et al.  Process route index (PRI) to assess level of explosiveness for inherent safety quantification , 2009 .

[3]  Faisal Khan,et al.  Inherent safety in offshore oil and gas activities: a review of the present status and future directions , 2002 .

[4]  Azmi Mohd Shariff,et al.  Inherent safety tool for explosion consequences study , 2006 .

[5]  Azmi Mohd Shariff,et al.  Qualitative Assessment for Inherently Safer Design (QAISD) at preliminary design stage , 2010 .

[6]  G Zwetsloot,et al.  Encouraging inherently safer production in European firms: a report from the field. , 2000, Journal of hazardous materials.

[7]  A. G. Rushton,et al.  Inherent safety and computer aided process design , 1994 .

[8]  Dennis C. Hendershot,et al.  Advances in inherent safety guidance , 2008 .

[9]  Faisal Khan,et al.  I2SI: A comprehensive quantitative tool for inherent safety and cost evaluation , 2005 .

[10]  Reginald B. H. Tan,et al.  Expert system for the design of inherently safer processes. 1. Route selection stage , 2002 .

[11]  Azmi Mohd Shariff,et al.  Inherent risk assessment—A new concept to evaluate risk in preliminary design stage , 2009 .

[12]  Hiroshi Koseki,et al.  Thermal characteristics and their relevance to spontaneous ignition of refuse plastics/paper fuel , 2009 .

[13]  J. P. Gupta,et al.  A simple graphical method for measuring inherent safety. , 2003, Journal of hazardous materials.

[14]  Trevor Kletz Plant Design For Safety: A User-Friendly Approach , 1990 .

[15]  Duncan Lawrence,et al.  Quantifying inherent safety of chemical process routes , 1996 .

[16]  Altshuller Creativity As an Exact Science , 1984 .

[17]  Markku Hurme,et al.  Comparison of inherent safety indices in process concept evaluation , 2005 .

[18]  D. C. Hendershot,et al.  Process minimization: Making plants safer , 2000 .

[19]  F. Crawley Offshore loss prevention , 1995 .

[20]  Azmi Mohd Shariff,et al.  Inherent safety index module (ISIM) to assess inherent safety level during preliminary design stage , 2008 .

[21]  T. Al-Hassan,et al.  Optimizing safety by inherent offshore platform design , 1996 .