Abstract

The classical theory of the precoat filtration with body-feed suggests the Carman equation obtained by integration of the Darcy ODE with constant pressure. Hereinafter the equation obtained in Part I by mean a mathematical modelling of the precoat filtration with body-feed in more realistic conditions of variable pressure was re-called and an experimental validation was done. A pilot filter equipped with a small centrifugal pump was used. The experimental results of the curve of filtrate volume vs. filtration time were compared both with the new equation curve and the Carman equation curve. In the specific conditions of laboratory testing, the estimation error in the filtration time with the new equation is -3.7%, while the estimation error with the classical Carman equation is -21.6%. But with higher permeability conditions of the filtration layer the error with Carman equation can greatly increase, as it was contemplate in Part I. The precoat filtration with body-feed must be followed by the filter cleaning. The research of an optimization of the filtration-cleaning cycle using the classic theory 7368 Dario Friso and Lucia Bortolini of filtration, and therefore the Carman equation, leads to the well known condition to have equal both filtration time and cleaning time. With the proposal of the new equation, in this work a new modelling of the cycle optimization was elaborated. It provided a ratio between filtration time and cleaning time always greater than 1 with values also up to 16 for the higher permeability of the filtering layer (reduced c     ). Therefore, the use of the previous optimization with a rate equal 1 is unacceptable with higher permeability, leading to a substantial halving of the filter productivity.

Highlights

  • In many fields of the agricultural and food engineering the precoat filtration with body-feed tends to be replaced by the Micro-filtration (MF) with membranes

  • In Part I [3], for the centrifugal pump used in industrial filters, it was possible to represent with high accuracy (R2=0.999) the flow rate-pressure V Pp experimental points of the pump curve with a parabola: Pp Pp max B V 2 (2)

  • After proposing in Part I [3] a mathematical modelling of the precoat filtration with body-feed and variable pressure, in this Part II the modelling represented by a new equation substituting the classical Carman equation was experimentally tested

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Summary

Introduction

In many fields of the agricultural and food engineering the precoat filtration with body-feed tends to be replaced by the Micro-filtration (MF) with membranes. The consequence of this situation is that the study of the precoat filtration with body-feed deserves still attention For this reason, in the Part I [3] the problem of the error associated with the use of the Carman equation was faced. It is known that the precoat filtration with body-feed is a discontinuous operation that needs the cleaning of the filter for which it was proposed an optimization to maximize the average flow rate of the full cycle. The result of this optimization was a relationship between the filtration time and the cleaning time with constant pressure [9]. Part II optimized the filtration-cleaning cycle, that is always to maximize the average flow rate of the full cycle and the productivity of the filter

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