IP Library Granted Patent US 10,450,424
Granted Patent B2
US 10,450,424 · App. 15/746,207 · Granted Oct 22, 2019

Process for producing dispersion of esterified cellulose ether

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Quick Facts
Patent No.
US 10,450,424
App. No.
15/746,207
Granted
Oct 22, 2019
Kind
B2
Abstract

A process for producing an aqueous composition comprising a dispersed esterified cellulose ether comprises the steps of grinding, in the presence of an aqueous diluent an esterified cellulose ether comprising (i) groups of the formula —C(O)—R—COOA or (ii) a combination of aliphatic monovalent acyl groups and groups of the formula —C(O)—R—COOA, wherein R is a N divalent aliphatic or aromatic hydrocarbon group and A is hydrogen or a cation, blending a salt of a fatty acid with the esterified cellulose ether and choosing the amounts of aqueous diluent, esterified cellulose ether and salt of a fatty acid that the produced aqueous composition comprises at least 20 percent of the dispersed esterified cellulose ether and heating the aqueous composition to a temperature of from 37 to 80 C during or after the grinding step.

Claims (16)

1. A process for producing an aqueous composition comprising a dispersed esterified cellulose ether comprising the steps of

grinding, in the presence of an aqueous diluent, at least one esterified cellulose ether comprising (i) groups of the formula —C(O)—R—COOA or (ii) a combination of aliphatic monovalent acyl groups and groups of the formula —C(O)—R—COOA, wherein R is a divalent aliphatic or aromatic hydrocarbon group and A is hydrogen or a cation,

blending at least one salt of a fatty acid and optionally one or more adjuvants with the esterified cellulose ether before, during or after the grinding of the esterified cellulose ether and choosing the amounts of aqueous diluent, esterified cellulose ether, salt of a fatty acid, and optionally one or more adjuvants that the produced aqueous composition comprises at least 25 percent of the dispersed esterified cellulose ether, based on the total weight of the aqueous composition, and

heating the aqueous composition to a temperature of from 37 to 80° C. during or after the grinding step.

2. The process of claim 1 wherein additionally an anionic surfactant comprising a sulfate or sulfonate group is blended with the esterified cellulose ether before, during or after the grinding of the esterified cellulose ether.

3. The process of claim 1 wherein the aqueous composition is heated to a temperature of from 40 to 70° C.

4. The process of claim 3 wherein the aqueous composition is heated to a temperature of from 40 to 55° C.

5. The process of claim 1 , wherein the aqueous composition is heated during a time period of at least 30 minutes.

6. The process of claim 1 , wherein the median particle size, d50, of the dispersed esterified cellulose ether particles is up to 7 micrometers, the median particle size, d50, being the size at which 50 volume percent of the particles have a smaller equivalent diameter and 50 volume percent have a larger equivalent diameter.

7. The process of claim 1 wherein the aqueous composition comprises at least 30 weight percent of said at least one dispersed esterified cellulose ether, based on the total weight of the aqueous composition.

8. The process of claim 1 wherein the aliphatic monovalent acyl groups in the esterified cellulose ether are acetyl, propionyl or butyryl groups, and the groups of the formula —C(O)—R—COOA are —C(O)—CH2-CH2-COOA, —C(O)—CH═CH—COOA, or —C(O)—C6H4-COOA groups.

9. The process of claim 1 wherein the esterified cellulose ether is hydroxypropyl methyl cellulose acetate succinate.

10. The process of claim 1 wherein the amount of the salt of a fatty acid is from 0.05 to 20 percent, based on the weight of the esterified cellulose ether.

11. The process of claim 1 wherein the salt of a fatty acid is an alkali metal or alkaline earth metal salt of stearic acid.

12. The process of claim 1 wherein the anionic surfactant comprising a sulfate or sulfonate group is a dialkyl sulfosuccinate.

13. The process of claim 1 wherein a film forming aid is added to the aqueous composition after heating the aqueous composition to a temperature of from 37 to 80° C.

Assignments (8)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 28, 2020
From: DDP SPECIALTY ELECTRONIC MATERIALS US, LLC.
To: NUTRITION & BIOSCIENCES USA 1, LLC
Reel/Frame 054533/0575 →
CHANGE OF LEGAL ENTITY Recorded Nov 28, 2020
From: DDP SPECIALTY ELECTRONIC MATERIALS US, INC.
To: DDP SPECIALTY ELECTRONIC MATERIALS US, LLC.
Reel/Frame 054530/0384 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 28, 2020
From: DOW GLOBAL TECHNOLOGIES LLC
To: THE DOW CHEMICAL COMPANY
Reel/Frame 054531/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 28, 2020
From: THE DOW CHEMICAL COMPANY
To: DDP SPECIALTY ELECTRONIC MATERIALS US, INC.
Reel/Frame 054533/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 13, 2019
From: KNARR, MATTHIAS; BRACKHAGEN, MEINOLF
To: DOW WOLFF CELLULOSICS GMBH & CO. OHG
Reel/Frame 049158/0917 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 13, 2019
From: FETNER, NEAL J.; ZHAO, JIN
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 049158/0995 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 13, 2019
From: DOW WOLFF CELLULOSICS GMBH & CO. OHG
To: THE DOW CHEMICAL COMPANY
Reel/Frame 049159/0068 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 13, 2019
From: THE DOW CHEMICAL COMPANY
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 049159/0145 →