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                                                                Cleaner Production
                water is taken entirely from group water boreholes within factory premises.
                                   3
                Approximately 35 m of drinking water is taken from the public network
                every day.
                Wastewater generation
                                                    3
                The factory generates about 16,000 m /day of industrial wastewater from
                different factory steams, including process effluents, boiler blow down, cool-
                ing water, vacuum water, and steam condensate. The wastewater is discharged
                to Akhnawy drain near the factory.
                CP opportunity assessment
                The main objective is to set cleaner production opportunities which were
                initially identified through an industrial audit of the factory (SEAM 1999a).
                The following improvement opportunities were identified as being of par-
                ticular importance:

                     • Upgrade loading and unloading procedures for oil ghee and fats to
                       minimize spillage.
                     • Improve housekeeping in the factory acids splitting unit.
                     • Improve oil recovery from processing unit effluents; especially oil
                       refining and packaging unit.
                     • Improve handling of animal fodder ingredients to prevent losses.
                     • Develop water consumption control, by installing water meters for
                       monitoring water consumption at various units, and installation of
                       self-closing taps to reduce water consumption in service units.

                CP techniques implemented/Cost/benefit analysis
                1. Source reduction was implemented through good housekeeping and preven-
                tive maintenance through upgrading loading and unloading procedures. During
                the loading and unloading of oil, significant levels of leakage and spillage of
                ghee and fatty matter from batch reactors and separators were occurring. These
                losses were entirely eliminated as a result of issuing improved procedural
                instructions and by improving the supervision of transfer operations.
                     The cost/benefit analysis for using this CP technique revealed the
                following:

                     • The implementation cost is nil.
                     • The annual saving is $3,6190.
                     • The payback period is immediate, which is considered encouraging
                       for investors.

                     2. Equipment modification was made through the installation of three
                gravity oil separators (GOS) manufactured by the factory. The GOSs were
                installed on the oil washing line, immediately after the point where water is
                recovered from the oil and ghee refining batch reactor. Recovered oil and ghee
                was discharged and lost to refinery effluent before the installation of the
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