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NPSH available calcTable 2: NPSHA calculationDen<strong>sit</strong>y kg/m 3 input 820Total Delta head friction m input 3.09Height liquid in tankabove pumpm input 2Vapour pressure mbar input 0featureHead vapour pressure m calc 0Atm pressure m calc 12.43NPSH available m calc 11.34modification can be carried out easily.There are two types of suction nozzlein a normal tank design. One type is thedouble ends design with flange at eachend. The other type only comes with anexternal nozzle. Refer <strong>to</strong> Figures 2a and2b <strong>for</strong> the proposed modification of thetank nozzle <strong>for</strong> the above mentioned typeof nozzles. nFigure 1: Isometric piping from tank <strong>to</strong> productpumpFigures 2a and 2b: Tank nozzle modificationA Predictive Method in Analysing Past Data –A Real Case on Production Line Setup Timeby Ir. Gan Chun ChetThere are many data collected that need <strong>to</strong>be analysed <strong>to</strong> determine whether a predictionis possible. Many methods can be applied <strong>to</strong>predict one data ahead of the previous data.The purpose of knowing one step ahead is <strong>to</strong>determine if the prediction of the next numberis a true number so that people can rely on it.Some judgments are blurred by the fact thatit is only a guess. The accuracy of the nextnumber is not known until it occurs.There are several methods that canbe applied <strong>to</strong> determine if a prediction isaccurate. Keep in mind that prediction error isanother fac<strong>to</strong>r that has <strong>to</strong> be considered be<strong>for</strong>ea decision is made. Otherwise, a predictionvalue is simply accepted in blind faith. Twosimple methods are listed here which could beused in a real application.• Moving Average• Exponential Smoothing Graph 1: Machine set-up time trendJurutera May <strong>2009</strong>11

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