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Fu r t h e r A p p l i c a t i o n s  o f  P r o c e s s I n t e g r a t i o n   125


                     thereby forming the Hydrogen Pinch. Separating the hydrogen
                     source and sink parts then determines the target value for the
                     hydrogen utility minimum flow rate.
                        The procedure for calculating the supply target requires varying
                     the flow rate of gas supplied to the system until a Hydrogen Pinch
                     is found. The sources from hydrogen-consuming processes or
                     from processes generating hydrogen as a secondary product
                     (dehydrogenation plants) have flow rates that are determined by
                     normal process operation; these rates are assumed to be fixed for the
                     purposes of designing a hydrogen network. However, process
                     hydrogen sources with variable flow rates can be regarded as
                     imports from external suppliers and from processes (i.e., steam
                     reformers or partial oxidation units) that generate hydrogen as a
                     main product. Those sources are hydrogen utilities.
                        One approach to minimizing hydrogen utility consumption is to
                     increase the purity of one or more sources. A hydrogen purification
                     system introduces an additional sink (feedstock for purification) and
                     two sources (purified stream and residue stream), resulting in new
                     targets. By employing Hydrogen Pinch Analysis, an engineer can
                     make the best use of hydrogen resources in order to meet new
                     demands and improve profitability.

                6.2  Oxygen Pinch Analysis

                     Another extension of Process Integration is Oxygen Pinch Analysis
                     (Zhelev and Ntlhakana, 1999). The idea is to analyze the problem so
                     that targets are derived prior to designing a system for minimizing
                     oxygen consumption of the micro-organisms used for waste
                     degradation. The next step is to design a flowsheet that achieves the
                     targets. In most cases, oxygen is supplied through agitation.
                     Aeration requires energy, so an analysis based on the Oxygen Pinch
                     eventually leads back to the original application of energy
                     conservation. Using the chemical oxygen demand or COD (Monod,
                     1949) as the baseline range for organic contaminants allows one to
                     set quantitative targets (for oxygen solubility, residence time, and
                     oxidation energy load) as well as additional qualitative targets—
                     namely, the growth rate that is a direct indicator of the age and
                     health of micro-organisms (Zhelev and Bhaw, 2000). Analyzing the
                     information in Figure 6.2 and then matching the oxygen supply line
                     to the CC (so they touch at the Pinch point) yields targeting information
                     on the growth rate of micro-organisms, oxygen solubility, residence
                     time, and oxidation energy load.
                        In the Oxygen Pinch approach, the method recurs to energy but
                     also incorporates extra information concerning environmental
                     issues. An important contribution of this method is its ability to
                     target—in parallel with the concentration of oxygen and the total
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