Introduction & Context

The pulper-finisher is a critical unit operation in food and chemical process engineering, specifically designed for the continuous, horizontal-axis centrifugal separation of solid-liquid mixtures. By utilizing a rotating screen basket and an internal scroll or paddle assembly, the machine separates fibrous solids (pulp) from the liquid phase (serum). This process is essential for applications such as tomato paste production, fruit juice extraction, and vegetable pureeing, where precise control over pulp moisture and particle size distribution is required to meet product quality standards.

Methodology & Formulas

The operational performance of a pulper-finisher is governed by the interaction between centrifugal acceleration, mechanical peripheral velocity, and the axial conveyance of the solid phase. The following formulas define the physical state of the system:

First, the angular velocity ω is derived from the rotational speed N:

\[ \omega = \frac{\pi \cdot N}{30} \]

The centrifugal force, expressed as a dimensionless multiple of gravity (G-force), is calculated using the basket radius and angular velocity:

\[ G = \frac{\omega^{2} \cdot \left( \frac{D}{2} \right)}{g} \]

The peripheral speed vt, which dictates the mechanical stress on the screen and the intensity of the separation, is defined as:

\[ v_{t} = \frac{\pi \cdot D \cdot N}{60} \]

The residence time τ, representing the duration the solid pulp remains within the machine to undergo dewatering, is determined by the machine length L and the axial conveyance speed v_{\text{scroll}}:

\[ \tau = \frac{L}{v_{\text{scroll}}} \]
Parameter Operational Regime / Limit Typical Range
G-Force Separation Efficiency 200 to 800
Peripheral Speed Mechanical Stress Limit 8 to 25 m/s
Screen Aperture Particle Cut-point 0.5 to 2.0 mm
Residence Time Dewatering Capacity 30 to 180 s