Particle degradation:Particle breakage

Particle degradation

Introduction

In some bulk solids handling processes intentional breakdown of the material is required, as in crushing, grinding and comminution. In many handling and storage situations, however, unintentional breakage occurs. This is usually termed degradation or attrition, depending on the mechanism of particle breakage. Bulk materials, when pneumatically conveyed, will impact against bends in the pipeline, and there may be a significant amount of particle to particle interaction. There may also be frequent impacts against the pipeline walls, and particles sliding along the pipeline walls in low velocity dense phase flows. These collisions and interactions will produce forces on the particles that may lead to their breakage.

Particle breakage

If particle breakdown occurs easily the bulk solid is said to be friable. Tendency to par- ticle breakdown covers three main situations. The first is a tendency to shatter or degrade when the bulk solid is subject to impact or compressive loading. The second is the tendency for fines and small pieces to be worn away by attrition when bulk solids either rub against each other or against some surface, such as a pipeline wall or bend. The third is the tendency for materials such as nylons and polymers to form angel hairs when conveyed, as a result of micro-melting occurring, due to the frictional heat of particles sliding against pipeline walls.

Of all conveying systems, dilute phase probably results in more material degrad- ation and attrition than any other. This is because particle velocity is a major variable in the problem and, in dilute phase conveying, high velocities have to be maintained. The potential influence of a pneumatic conveying system on a material is demonstrated in Figures 24.1 and 24.2. This is a consequence of conveying a friable material at an excessively high velocity in dilute phase suspension flow in a conveying system with a large number of small radius bends.

Figure 24.1 shows the influence on the cumulative particle size distribution for the material before and after conveying. The mean particle size, based on the 50 per cent value, has changed from about 177–152 µm. The really significant effect, however, is shown in the fractional size distribution plot in Figure 24.2. In this magnified plot the effect of degradation on the material can be clearly seen. A considerable number of+

Particle degradation-0038

fines are produced and even on a percentage mass basis these cause a significant sec- ondary peak in the particle size distribution.

Incoming search terms:

Related posts:

Financial justification:Capital cost savings
Compressed Air Transmission and Treatment:Inducted contaminants
Compressed Air Transmission and Treatment:Water vapour
Gas–solid separation devices:Separation devices and Gravity settling chambers.
Low pressure and vacuum:Feeding requirements and Flow metering.
Pipeline scaling parameters:Vertical pipelines
ROUBLESHOOTING PNEUMA TIC CIRCUITS:PNEUMATIC SYSTEM COMPONENT fAILURE MODES
RESERVOIRS, STRAINERS, FILTERS, AND ACCUMULATORS:Full-Flow Filters.
RESERVOIRS, STRAINERS, FILTERS, AND ACCUMULATORS:fiLTRATION
Hydraulic pumps:Pump performance
Hydraulic coolers and heat exchangers.
Air Compressors, Air Treatment and Pressure Regulation:air treatment
Sequencing Applications:Pressure-controlled sequences
ENTROPY:REVERSIBLE STEADY-FLOW WORK
HEAT EXCHANGERS:TYPES OF HEAT EXCHANGERS

Leave a comment

Your email address will not be published. Required fields are marked *