rdf-syntax-grammar
mods:
  schema location: http://www.loc.gov/mods/v3 http://www.loc.gov/standards/mods/v3/mods-3-2.xsd
  title info:
    non sort: The
    title: integration of Dow's Fire and Explosion Index into process design and optimization to achieve an inherently safer design
  name:
    name part: Suardin, Jaffee
    name part: 1977-
    role:
      role term: creator
  name:
    name part: Mannan, Mahboobul Sam
    role:
      role term: thesis advisor.
  type of resource: text
  genre: bibliography
  origin info:
    place:
      place term: txu
    date issued: 2006
    issuance: monographic
  language:
    language term: eng
  physical description:
    form: electronic
    form: remote
  abstract: The integration of the safety parameter into process design and optimization is essential. However, there is no previous work in integrating the fire and explosion index (F&EI) into design and optimization. This research proposed a procedure for integrating safety into the design and optimization framework by using the safety parameter as optimization constraint. The method used in this research is Dow's Fire and Explosion Index which is usually calculated manually. This research automates the calculation of F&EI. The ability to calculate theF&EI, to determine loss control credit factors and business interruption, and to perform process unit risk analysis are unique features of this F&EI program. In addition to F&EI calculation, the F&EI program provides descriptions of each item of the penalties, chemicals/materials data bases, the flexibility to submit known chemical/material data to data bases, and material factor calculations. Moreover, the sensitivity analyses are automated by generating charts and expressions of F&EI as a function of material inventory and pressure. The expression will be the focal point in the process of integrating F&EI into process design and optimization framework. The proposed procedure of integrating F&EI into process design andoptimization framework is verified by applying it into reactor-distillation column system. The final result is the optimum economic and inherently safer design for the reactor and distillation column system.
  note: by Jaffee Suardin.
  note: "Major Subject: Chemical Engineering"
  note: Title from author supplied metadata (automated record created on Feb. 23, 2007.)
  note: Vita.
  note: Abstract.
  note: Electronic resource.
  note: Mode of access: World Wide Web.
  note: System requirements: World Wide Web access and Adobe Acrobat Reader.
  note: M. S. Texas A&M University 2005.
  note: Includes bibliographical references.
  note: Text (Thesis).
  subject:
    topic: Major chemical engineering
  subject:
    topic: process safety
  subject:
    topic: process design
  subject:
    topic: inherently safer design
  subject:
    topic: dow's fire and explosion index
  subject:
    topic: process optimization
  identifier: http://hdl.handle.net/1969.1/4145
  record info:
    record content source: TXA
    record creation date: 070326
    record change date: 20151104165119.0
    record identifier: in00002229451