Process for dry-grinding a polysaccharide derivative
View Patent ↗In a process for producing a particulate polysaccharide derivative by dry-grinding a moist polysaccharide derivative the median length of the particles after dry-grinding is controlled by controlling the moisture content of the polysaccharide derivative prior to dry-grinding. Advantageously the median length of the particles after dry-grinding is adjusted to a first value by a first moisture content of the polysaccharide derivative prior to dry-grinding and is adjusted to a second value by a second moisture content.
1. A process for producing a particulate polysaccharide derivative by dry-grinding a moist polysaccharide derivative wherein the median length of the particles after dry-grinding is controlled and adjusted by controlling and adjusting the moisture content of the polysaccharide derivative prior to dry-grinding in a gas-swept impact mill.
2. The process of claim 1 wherein the median length of the particles after dry-grinding is adjusted to a first value by a first moisture content of the polysaccharide derivative prior to dry-grinding and is adjusted to a second value by a second moisture content.
3. The process of claim 1 wherein the dry-grinding is conducted in a rotational dry-grinding device and the median length of the particles after dry-grinding is controlled by controlling the circumferential speed of the dry-grinding device, in addition to controlling the moisture content of the polysaccharide derivative prior to dry-grinding.
4. The process of claim 1 comprising the steps of
a) dry-grinding at least three samples of a moist polysaccharide derivative, each sample having a different moisture content prior to dry-grinding, and measuring the median length of the particles after dry-grinding of each of the samples,
b) determining the correlation between the median length of the particles after dry-grinding and the moisture content of the polysaccharide derivative prior to dry-grinding, and
c1) adapting the moisture content of the polysaccharide derivative prior to dry-grinding to the desired median length of the particles after dry-grinding.
5. A process for producing a particulate polysaccharide derivative by dry-grinding a moist polysaccharide derivative in a gas-swept impact mill wherein the moisture content of the moist polysaccharide derivative prior to dry-grinding is determined by measuring the median length of the particles after dry-grinding.
6. The process of claim 5 comprising the steps of
a) dry-grinding at least three samples of a moist polysaccharide derivative, each sample having a different moisture content prior to dry-grinding, and measuring the median length of the particles after dry-grinding of each of the samples, and
b) determining the correlation between the median length of the particles after dry-grinding and the moisture content of the polysaccharide derivative prior to dry-grinding, and
c2) applying the correlation resulting from step b) to a moist polysaccharide derivative for determining the moisture content of the polysaccharide derivative prior to dry-grinding by measuring the median length of the particles after dry-grinding.
7. The process of claim 5 wherein the determined correlation between the median length of the particles after dry-grinding and the moisture content prior to dry-grinding is used as in-process control in a continuous dry-grinding process wherein the median length of dry-ground particles is determined and used for setting and optionally adapting the moisture content of the polysaccharide derivative prior to dry-grinding.
8. The process of claim 7 wherein the in-process control is carried out on-line.
9. The process of claim 1 wherein the determination or control of the moisture content of the polysaccharide derivative prior to dry-grinding is used for controlling the bulk density of the particles after dry-grinding.
10. The process of claim 1 wherein the polysaccharide derivative has been obtained by separating a polysaccharide derivative from a suspension thereof in a liquid and is subsequently subjected to dry-grinding in a dry-grinding device.
11. The process of claim 1 wherein a dry polysaccharide derivative and a liquid are mixed in a compounder and the thus obtained moist polysaccharide derivative is subsequently subjected to dry-grinding in a dry-grinding device.
12. The process of claim 1 wherein the polysaccharide derivative has a moisture content of 30 to 98 percent prior to dry-grinding and the moisture content is reduced to 1 to 20 percent after dry-grinding, based on the total weight of the moist polysaccharide derivative.
13. The process of claim 1 wherein the median length of the particles is determined by high speed image analysis.
14. The process of claim 5 wherein the determination or control of the moisture content of the polysaccharide derivative prior to dry-grinding is used for controlling the bulk density of the particles after dry-grinding.
15. The process of claim 5 wherein the polysaccharide derivative has been obtained by separating a polysaccharide derivative from a suspension thereof in a liquid and is subsequently subjected to dry-grinding in a dry-grinding device.
16. The process of claim 5 wherein a dry polysaccharide derivative and a liquid are mixed in a compounder and the thus obtained moist polysaccharide derivative is subsequently subjected to dry-grinding in a dry-grinding device.
17. The process of claim 5 wherein the polysaccharide derivative has a moisture content of 30 to 98 percent prior to dry-grinding and the moisture content is reduced to 1 to 20 percent after dry-grinding, based on the total weight of the moist polysaccharide derivative.
18. The process of claim 5 wherein the median length of the particles is determined by high speed image.