05.03.2014 Views

Strona 2_redak - Instytut Agrofizyki im. Bohdana Dobrzańskiego ...

Strona 2_redak - Instytut Agrofizyki im. Bohdana Dobrzańskiego ...

Strona 2_redak - Instytut Agrofizyki im. Bohdana Dobrzańskiego ...

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

94<br />

unconfined yield strength to powder density 1 c was used as a measure of flowability,<br />

a low degree of consistence with the direct shear test was observed, particularly at low<br />

range of normal pressure. At higher levels of normal pressure, both the methods gave<br />

fairly close results. The authors [16] performed a ranking of a number of materials<br />

based on the Jenike and Johanson methods and found that the two methods gave<br />

results in a fairly good agreement. In summary, Johanson’s indcizer was found to<br />

be a convenient and repeatable tool to use, but its predicted 1 c values and arching<br />

and rathole diameters did not correlate well with the results of the Jenike cell. For<br />

some materials good agreement of flowability ranking was obtained under certain<br />

circumstances, but the basis for these l<strong>im</strong>iting circumstances could not be quantified.<br />

JR Johanson Inc. proposed investigations of materials in a wide range of<br />

temperature and moisture content. Standard testing has been offered for determination<br />

of density, permeability, strength and angles of friction and adhesion.<br />

Testing of flowability using Johanson’s indices is also offered. Values of parameters<br />

for determination of the indices are measured under pressures and for scale<br />

factors corresponding to the d<strong>im</strong>ensions of equipment applied in the process<br />

under consideration. Some indices have physical d<strong>im</strong>ensions expressed in US<br />

units, as for that market the equipment was meant.<br />

The Arching Index (AI), with a typical range of 0-4 ft (1.22 m), is the conical<br />

hopper outlet required for unaided gravity flow after dropping the solids into an<br />

empty hopper and ensuring arch collapse in a conical bin. The AI is related with<br />

material properties as follows: AI = 2.21 c /, where 1 c i are measured under normal<br />

consolidation pressure of: 3d/2.<br />

The Ratholing Index (RI) – typical range, 0-30 ft (0 to 9.15 m) – is the flow<br />

channel size in a hopper required for a solid to collapse into the hole above the<br />

outlet, if arching did not occur. RI also provides a good indication of lumping<br />

tendency. If, after a t<strong>im</strong>e at rest, the solids RI exceeds 10 ft (3.05 m) a lump breaker<br />

may be needed in the system. The RI is related with material properties as follows:<br />

RI = 2.51 c where 1 c DQGDUHPHDVXUHGDWFRQVROLGDWLRQSUHVVXUHRId.<br />

The Hopper Index (HI) is the min<strong>im</strong>um half-angle of a conical hopper, required<br />

to ensure flow along the hopper walls. Its value is HI = 42 –3where –3 is the<br />

angle of kinetic friction measured at nRUPDO FRQVROLGDWLRQ VWUHVV RI d, or if 3<br />

increases with an increase in stress value of 3 determined at the stress level of D.<br />

The Flow Rate Index (FRI) – typical range 1-12000 lb min -1 (0.5 to 5400 kg min -1 )<br />

is the rate at which the solid will flow through a hopper outlet of diameter d when<br />

totally deaerated. Low value of FRI usually points out to fine, highly compressible<br />

powder. Particles of sizes in excess of 400 m are usually incompressible, very<br />

permeable, and have a high FRI. Variation in the value of the index may be a signal<br />

of segregation or change in composition of powder mixture during processing.

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!