Page 106 - Design of Simple and Robust Process Plants
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4.2 The Methodology of Process Synthesis  91
                 4.2.1
                 Reaction


                 4.2.1.1  Evaluate raw materials, reactants and products and the chemical reaction
                The first decision to be taken is that of which feed streams are to be selected for the
                 main reaction, in addition to other purposes such as solvent, anti-oxidant, inhibitor,
                 neutralizing agent, and the physical state of the materials. All of these chemicals
                 must to be evaluated on:

                   .  Purpose
                   .  Safety ± internal as well as external
                   .  Environmental
                   .  Transportation mode, storage, and its physical state
                   .  Integration in relation to other processes
                   .  Purity and concentration
                These steps are often under estimated, although a large proportion of the costs are
                 logistic cost which are determined ± but not yet quantified ± at this stage. Some of
                 these materials are not selected at this point, though it is possible to discuss them
                 here as they all have to pass the same rationale.
                   .  The purpose often leaves us alternatives: for example, if we want to neutralize
                      with a base, there are often more alternatives such as caustic solution or pel-
                      lets, lime, NH 3, a weak inorganic or an organic base. Similar choices are to
                      be made for acid neutralization. In most applications alternatives are avail-
                      able, including the main reactants. List all these alternatives from economic,
                      safety and environmental perspectives ± and do not forget to list the form/
                      concentration of supply.
                   .  Apply the inherently safer and environmentally sound design philosophies at
                      this stage to their full extent. It is at this point when there is the major impact
                      on the safety and environmental aspects of an operation. A striking example
                      of this is the selection of a chemical: in an operational facility, seawater was
                      used for direct cooling of process streams, but the seawater needed to be trea-
                      ted to overcome the growth of mussels within the exchangers. Although the
                      solution was to add chlorine, it was unnecessary to highlight the inherent
                      danger of having chlorine on site; rather, a solution of sodium hypochlorite
                      was found to be a suitable replacement.
                   .  Transportation and storage each have major impacts on the design. The exam-
                      ple of the batch plant in Figures 1. 4±1.7 in Chapter 1 clearly shows the
                      increase and decrease of storage facilities during the process' evolution. The
                      practice of transporting a dosing agent in dedicated containers in a liquid
                      form at a concentration level for easy handling is to be preferred. It should be
                      recognized that handling operations can lead to mishaps and are to be mini-
                      mized.
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