3. CASE STUDY A mio t/a cement plant is having a closed circuit ball mill for cement grinding: The mill has been operating with satisfactory performance interms of system availability and output, however power consumption was on higher side. System Description Mill Rated capacity 150 t/h OPC at 2800 blaine I chamber liners
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WhatsAppLow pressure pump of cement mill Low pressure pump of cement mill; The low vent volume through the bag filter is mainly due to very high pressure drop across the bag filter 180200 mmWG The actual flow measured is only 4% of the total separator air Mill was crash stopped for collection of chamber samples to evaluate size reduction progress in side the mill.
WhatsAppPump Head = 0 if no pump present The pressure drop or rather pressure difference dP (it could be a gain) between the start and the end of a pipe is therefore given by this equation: dP = Friction Loss + Fittings Loss + Component Loss Elevation[startend] Pump Head where P[end] = Pressure .
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WhatsAppCALCULATE THE PRESSURE HEAD ANYWHERE ON THE SUCTION SIDE OF THE PUMP We can determine the pressure head anywhere on the suction side of the pump by the same method. In this case, ∆H P = 0 since there is no pump within the control volume (see Figure 4). ∆H P = 0 and subscript 2 is replaced with subscript X in equation [4].
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