Educ. Reso. for Part. Techn. 992Q-Bates
<http://www.erpt.org/992Q/bate-00.htm>
Copyright © 1999 ERC at the Univ. of Florida

Problems in Particulate Flow, Part A -- Flow Regimes, by Lyn Bates

-- 1. Introduction --


The controlled flow of particulate solids is a fundamental requirement for reliable and efficient operation of virtually all bulk storage, handling and processing installations. The scale and manner of bulk storage and the means to regulate the flow of solids rates varies widely. So do the ways in which flow reliability, flow uniformity and feed accuracy deviate from required standards of performance. Despite advances in powder technology, many types of problems arise in the field of storage and feeding of bulk materials. The root of these problems is that loose solids exist in a vast range of conditions and possess wide-ranging and complex rheological properties. These inherent difficulties are further aggravated by the multitudinous duties and extensive range of ambient conditions that have to be accommodated in industrial applications.

The key to efficient storage and feeding of bulk solids is securing reliable and consistent flow.

When the chosen material is free flowing and in a suitable condition under all conditions of use, control of the flow rate is usually simple. Difficulties in solids feeding mainly revolve around attaining a stable density and a satisfactory flow state of the material being handled. Good design is founded upon a systematic understanding of powder behaviour, flow patterns and equipment mechanics. Means to achieve this end are explored in these papers, together with a review of the varied forms of problems that are commonly encountered and how these may be resolved.


-- 2. Specification of Bulk Solids for Storage and Handling --


A prerequisite of any design study and a sound basis for plant specification, is to establish firm parameters for the duty and specification of the equipment. Whilst flow related properties of bulk solids can be measured, they rarely figure in contractual documents connected with the specification for supply of solids storage and handling equipment for various reasons. In some cases the material is not available for testing before production commences. Powder testing devices are not widely available and sometime the cost of comprehensive tests is not considered viable in relation to the equipment value. More usually however, the method adopted is to provide the name and a brief description of the material, and supply 'typical' samples on request.

These handicaps to a scientific approach are exacerbated by the host of features that characterise how a bulk material will behave within a particular storage and handling situation.

Basic information as to bulk density and wall friction are relatively simple to define and measure. Information as to the bulk strength and deformation behaviour of a bulk solid is inherently more complex. Fundamental to the problem is that there is no single or 'once only' flow property measurement for any given bulk material. Even if there were one for given conditions, the interaction of equipment geometry, materials of construction, and variables of operation and environmental conditions, could lead to this generalised information being misleading. It is most important to appreciate that measurements of the flow properties of a bulk materials refer only to one specific condition of the material, and that any physical change in the material totally invalidates the design value of these measurements. Tests must be conducted for different product conditions if the material is likely to vary in any physical manner, such as particle size composition or moisture content, and measurements taken for the 'worst' condition used as a basis for relevant design features.

Also note that the characteristics of interest differ widely according to the application. Aspects of material quality and hygiene, safety and operator considerations, features of the site and preferred form of equipment are all application related. The supply consistency of the bulk material must also be taking into account. The effect of multiple sourced products, operation and process variables, constituent changes, homogeneity of the bulk and the stability of the material with time or ambient variables, are vitally important with respect to how the material will behave.

To address this awkward situation the Bulk Solids Handling Committee of the Institution of Mechanical Engineers produced a document, setting out a format for the specification of bulk solids for storage and handing purposes [I. Mech. E. 1996]. The publication includes basic fact sheets (Tables 1 and 2), supplemented with queries concerning differing features of possible interest.


Table 1. SPECIFICATION OF A BULK SOLID

for a storage or mechanical handling application
(as recommended by the I. Mech. E. Bulk Materials Handling Committee)

Client/Ref . . . . . . . . . . . . . .

Process Duty . . . . . . . . . . . . .
. . . . . . . . . . . . . . . . . . . . . .
. . . . . . . . . . . . . . . . . . . . . .

Special Ambient Condition
. . . . . . . . . . . . . . . . . . . . . .

Company . . . . . . . . . . .

Location . . . . . . . . . . .
. . . . . . . . . . . . . . . . . . . . . .
. . . . . . . . . . . . . . . . . . . . . .

Equipment under consideration
. . . . . . . . . . . . . . . . . . . . . .

Properties of the Bulk Material
- Generic Name
- Source or Sample
- Trade Name
- Size of Sample
- Clients Ref
- Date of Sample

Individual Product - Yes/No

Description
- Appearance
- Colour
- Ambient Temp . . . . oC
- Texture

Uniformity
- Homogeneous - Yes/No
- Stable - Yes/No
- Consistent - Yes/No

Physical Composition
- Particle Size Range:
     Min . . . . . Max . . . . .
- Particle Shape

Moisture Content [W/W basis]
- Total . . . . %
- Free . . . . %
- Inherent . . . . %
- Bound . . . . %

Melting/Softening temperature

Density [kg/m]
- Loosely Poured . . . .
- Lightly Tapped . . . .
- Aerated . . . .
- Material Compactable - Yes/No

Flow Condition
- Free Flowing - Yes/No
- Cohesive - Yes/No
- Interlocking - Yes/No
- 'Cakes' - Yes/No

Pour angle of Repose
- Variable Yes/No
- degrees . . . . .

Slip Properties
- Contact Face
- Surface Finish
- Friction angle

Shear cell test results:

Particle size distribution:

Known handling problems:
. . . . . . . . . . . . . . . . . . . . . .

Sensitive product properties:

Any other relevant information:
. . . . . . . . . . . . . . . . . . . . . .

Signed: ______________________


Table 2. FEATURES OF THE BULK MATERIAL

The features are to be graded according to the following scales:

  IMPORTANCE
1 Insignificant
2 Significant
3 Important
4 Extreme
HAS EFFECTS ON
1 Health and Safety
2 Performance of the Equipment
3 Value or use of the Product
4 Design/Durability of Equipment
5 Environment
.

.

Segregates readily
Tends to 'Flood'
Cohesive / Sticky
Fibrous / Interlocking
Degrades / Deteriorates
Agglomerates
Abrasive

Melts at .... oC
Hygroscopic Deliquesces
Cakes / Sets Hardens
Reactive
Flammable
Explosive
Corrosive
Radioactive

Prevention of Contamination
High / Low Temperature
Ambient Gas
At Pressure ..... Bar

Hygiene requirements
Dusty, Dirty
Irritant
Odours / Fumes / Vapours
Toxic / Ingestion Hazard
Sharp / Penetrating
Unpleasant
Valuable

IMPORTANCE
Circle One Only
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4

1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4

1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4

1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4
1 2 3 4

HAS EFFECTS ON
Circle ALL relevant
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5

1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5

1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5

1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5
1 2 3 4 5

Please supply all fire, safety, health, and environmental
impact information and any other relevant details.


Quantified values are essential for predictable designs and tend to figure increasingly with quality programmes and design verification procedures. There remain certain features that are judgement related and essentially must fall within the province of the user to rank as to their importance. For these it is necessary to utilise a grading system indicating the degree to which the suitability of equipment may be effected. Whereas some aspects may not be relevant in particular cases, a systematic review of this type prompts attention so that no feature is overlooked by default. Guide notes outlining test procedures and their relevance are also included in the publication.

Two comprehensive studies of plants that handle bulk solids have shown that their performance efficiency compares very unfavourably with plants handling liquids and gasses [Merrow 1981 and 1985]. More significantly, this discrepancy has shown little signs of improvement compared with plant built in the sixties, despite the advances made in bulk technology since that time. It is clear that steps taken to introduce the use of more quantified values for equipment design must progress alongside the diffusion of knowledge in particulate solids technology, for performance standards to improve in the ubiquitous industries that handle bulk solids. Hence, one reason for this article and the means adopted for its propagation.


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