Process for producing cellulose derivatives of high bulk density and good flowability
US-9352330-B2 · May 31, 2016 · US
US2016256390A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016256390-A1 |
| Application number | US-201615140786-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 23, 2016 |
| Priority date | Apr 6, 2011 |
| Publication date | Sep 8, 2016 |
| Grant date | — |
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A particulate cellulose derivative is obtained in a process of grinding and drying a moist cellulose derivative which comprises the steps of A) providing a cellulose derivative having a moisture content of from 60 to 95 percent, based on the total weight of the moist cellulose derivative, B) grinding and partially drying the moist cellulose derivative in a gas-swept impact mill; and C) contacting the ground and partially dried cellulose derivative with an additional amount of a drying gas outside the gas-swept impact mill. The obtained particulate cellulose derivative has a high untapped bulk density and a good flowability.
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1 .- 10 . (canceled) 11 . A particulate cellulose derivative having a median Equivalent Projected Circle Diameter (EQPC) of less than 140 micrometers, an untapped bulk density of at least 0.40 g/cm 3 and a Carr Index of 30 or less. 12 . The particulate cellulose derivative of claim 11 having a Carr Index of 25 or less. 13 . The particulate cellulose derivative of claim 11 having a median particle length of from 60 to 350 micrometers. 14 . The particulate cellulose derivative of claim 11 having an onset dissolution temperature of at least 61.5° C. 15 . A dosage form produced from a) one or more cellulose derivatives of claim 11 , b) one or more active ingredients, and c) one or more optional adjuvants. 16 . (canceled) 17 . The particulate cellulose derivative of claim 11 being one of methyl cellulose, methyl hydroxyethyl cellulose, methyl hydroxypropyl cellulose and hydroxypropyl cellulose. 18 . The particulate cellulose derivative of claim 11 being hydroxypropyl methylcellulose. 19 . The particulate cellulose derivative of claim 11 having an untapped bulk density of at least 480 g/l. 20 . The particulate cellulose derivative of claim 18 having a Carr Index of 25 or less and a median particle length of from 60 to 350 micrometers.
Post-etherification treatments of chemical or physical type, {e.g. mixed etherification in two steps}, including purification · CPC title
with organic macromolecular compounds · CPC title
Mixed ethers, i.e. ethers with two or more different etherifying groups · CPC title
Ventilating, or influencing air circulation · CPC title
Passing gas through crushing or disintegrating zone ({B02C15/001}, B02C23/38, B02C23/40 take precedence) · CPC title
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