Method of making granules and the granulator

a technology of granules and granules, which is applied in the direction of granulation in rotating dishes/pans, presses, manufacturing tools, etc., can solve the problems of difficult to obtain accurately metered amounts of finely divided materials into a tablet die, granules that have low compactness and redisperse easily, and the rate limiting step in the production process has been found to be the extrusion stag

Inactive Publication Date: 2003-06-24
CROP CARE AUSTRALASIA PTY LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In practice in the pharmaceutical industry, it has been found that it is difficult to obtain accurately metered amounts of finely divided materials into a tablet die, because of the inconsistent flow characteristics of finely divided materials.
These granules typically have low compactness and redisperse readily.
While WG granules prepared using the above described process have been successfully commercialized, the rate limiting step in the production process has been found to be the extrusion stage.
When the material is friable the sweeping action of the blades over the screen causes the material to be fractured and broken down in size.
In practice, in combination with the sweeping action, this causes frictional wear on the screen and the blade edge.
This pressure requirement also means adjustment to provide uniform pressure across the working area is difficult as the characteristics of the plastic material may change from batch to batch and also with temperature.
In the case of the Jackson-Crockatt apparatus with the reciprocating rotating blade, if the diameter of the screen and area of the working surface is increased to increase productivity, the tip speed of the blade is increased which can lead to difficulties in satisfactory operation.
For example, it is more difficult to achieve satisfactory alignment of the blade and screen.
Furthermore, because of higher tip speeds heat build up can cause problems.
Accordingly it is not practical to increase the diameter to the extent desired and as set out above the granulator is usually the rate limiting step in granulation processes.
However in the agrochemical industry where larger quantities of granules are required to be processed, this can be a major problem.
Furthermore, as mentioned above, the screen can wear and become damaged leading to unacceptably coarser extrudate being formed and the manufacturing process having to be interrupted and the screen replaced with obvious production and cost penalties.
While achieving good performance with such reciprocating action some unevenness in wear on the screen can occur because the circumferential pathway is not fully used.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 2

This is a comparative example that illustrates extrusions using a commercial granulator.

5 kg of a wet simazine mix identical to that described in Example 1 was prepared and passed through a No. 7 Jackson Crockatt granulator but in its unmodified configuration. It was fitted with the same 910 .mu.m aperture mesh and base plate used for Example 1 but the standard 3 blade Jackson Crockatt rotor replaced the rollers used in the granulator of Example 1. The extent and speed of reciprocation were the same as that of Example 1.

The wet mix was extruded satisfactorily and was converted to granules in accordance with the method described in Example 1. 95.4% of the dry granules by weight were in the size range of 0.5-1.7 mm. The extrusion rate was 54 kg / Hr and the rate per 1000 mm.sup.2 of exposed mesh was 3.3 kg / Hr which is significantly less than the rate in Example 1.

example 3

This Example illustrates the granulation of sodium lauryl sulfate detergent using a laboratory scale model of a granulator according to the invention.

A laboratory granulator was manufactured to be similar to the unit described in Example 1. It was made from stainless steel and consisted of a vertical cylindrical hopper of 75 mm internal diameter with 3 steel rollers, each 37 mm in diameter with a 12 mm wide smooth surface. The rollers were positioned an equal distance apart on steel support rods fixed at right angles to a reciprocating vertical shaft.

Granular sodium lauryl sulfate (Zoharpon SLS brand) was used.

A dry sieve analysis was carried out on the material as received, results as follows:

The detergent was first dry granulated adding it to the laboratory granulator fitted with a 910 .mu.m aperture woven stainless steel wire mesh tensioned over a perforated base plate. The roller assembly was adjusted so that the rollers were lightly tensioned on the mesh. The drive shaft recipr...

example 4

This Example illustrates the wet granulation of a commercial laundry detergent composition.

"Cold Power" distributed by Colgate-Palmolive Pty Ltd, was used.

A dry sieve analysis was carried out on a sample of "Cold Power" powder with the following results:

A wet mix was prepared by blending 200 g of "Cold Power" with 5 g of water. This was passed through the laboratory granulator described in Example 3. This was set up and operated in the same manner as described under Example 3. The wet mix extruded satisfactorily to produce cohesive extrudates, generally 2-4 mm in length. More energy was required to extrude the "Cold Power" pre-mix than the sodium lauryl sulfate pre-mix of Example 3.

The wet extrudates were rolled / tumbled vigorously for 120 seconds by hand in an inflated polyethylene bag which reduced them to reasonably smooth elongated granules. After drying at 45.degree. C., 95.7% of the granules by weight were in the size range of 0.5-1.7 mm.

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PUM

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Abstract

A granulator comprising a perforate screen located within a housing, a roller having a curved convex outer surface wherein the roller is pivotable relative to the screen so that in operation plastic material is able to be forced through the perforate screen by the roller surface so the roller pivots. The granulator is useful for wet and dry granulation.

Description

FIELD AND BACKGROUND OF THE INVENTIONThis invention relates to granulators used for or as part of a process for reducing the size of materials to form granules. Granules are widely used in the food, cleaning detergent, mineral processing, agrochemical and pharmaceutical industries. In many applications they offer significant advantages over other types of formulations. For example, they are typically low dusting and also offer advantages of ease of clean up of spills.Granules may be prepared using a number of methods including agglomeration, spray drying and size reduction.The term granulator is applied generally to equipment that may be used to produce granules. However, more particularly it is usually used to refer to special equipment specifically designed or modified for producing granules.In the pharmaceutical industry granulation is a standard step that precedes tabletting. In practice in the pharmaceutical industry, it has been found that it is difficult to obtain accurately ...

Claims

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Application Information

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Patent Type & Authority Patents(United States)
IPC IPC(8): B01J2/20B30B11/22B01J2/14B29B9/08
CPCB30B11/228B01J2/20B29B9/08
Inventor KEY, EDWARD JOHN
Owner CROP CARE AUSTRALASIA PTY LTD
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