IP Library Granted Patent US 9,359,450
Granted Patent B2
US 9,359,450 · App. 14/009,430 · Granted Jun 7, 2016

Process for reducing the amount of water-insoluble fibers in a water-soluble cellulose derivative

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 9,359,450
App. No.
14/009,430
Granted
Jun 7, 2016
Kind
B2
Abstract

The amount of water-insoluble fibers in a water-soluble cellulose derivative is reduced in a process comprising the steps of a) providing a water-soluble cellulose derivative having a residual amount of at least 20 ppm by weight of water-insoluble fibers in a 2 weight percent aqueous solution of the water-soluble cellulose derivative; b) mixing the water-soluble cellulose derivative of step a) with a liquid in a compounder to provide a moist water-soluble cellulose derivative having a temperature of at least 50 C and a moisture content of from 35 to 90 percent, based on the total weight of the moist cellulose derivative; and c) drying-grinding the mixture of step b) in a gas-swept impact mill to obtain a dried and ground cellulose derivative.

Claims (14)

1. A process for reducing the amount of water-insoluble fibers in a water-soluble cellulose derivative comprising the steps of

ai) treating cellulose with an alkali metal hydroxide to produce alkali cellulose,

aii) reacting the alkali cellulose with a derivatizing agent to produce a water-soluble cellulose derivative, and

aiii) washing the water-soluble cellulose derivative with a washing liquor having a temperature of 65 to 95° C. to remove by-products with or without a subsequent drying step but in the absence of a grinding step,

to provide a water-soluble cellulose derivative having a residual amount of at least 20 ppm by weight of water-insoluble fibers in a 2 weight percent aqueous solution of the water-soluble cellulose derivative;

b) mixing the water-soluble cellulose derivative of step a) with a liquid in a compounder to provide a moist water-soluble cellulose derivative having a temperature of at least 55° C. and up to 75° C. and a moisture content of from 50 to 75 percent, based on the total weight of the moist cellulose derivative; and

c) drying-grinding the mixture of step b) having a temperature of at least 55° C. and up to 75° C. in a gas-swept impact mill to obtain a dried and ground cellulose derivative, wherein the water-soluble cellulose derivative is a methylcellulose or a hydroxypropyl methylcellulose.

2. The process of claim 1 wherein in step iii) the water-soluble cellulose derivative is washed with a washing liquor to provide a water-soluble cellulose derivative having a moisture content of from 30 to 60 percent, based on the total weight of the moist cellulose derivative, and is mixed with an additional amount of liquid in step b).

3. The process of claim 1 wherein in step iii) the water-soluble cellulose derivative is washed with a washing liquor and subjected to drying to provide a water-soluble cellulose derivative having a moisture content of less than 30 percent, based on the total weight of the moist cellulose derivative, and is mixed with a liquid in step b).

4. The process of claim 1 wherein in step iii) the water-soluble cellulose derivative is washed with water.

5. The process of claim 1 wherein the water-soluble cellulose derivative has a residual amount of at least 150 ppm of water-insoluble fibers.

6. The process of claim 1 wherein the water-soluble cellulose derivative of step a) is mixed in step b) with a liquid in a compounder to provide a moist water-soluble cellulose derivative having a temperature of at least 58° C.

7. The process of claim 1 wherein in step b) aqueous liquid is used.

8. The process of claim 1 wherein the dried and ground cellulose derivative is subjected to gas classification.

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 Apr 29, 2016
From: GOERLACH-DOHT, YVONNE M.; HERMANNS, JUERGEN
To: DOW STADE PRODUKTIONS GMBH & CO. OHG
Reel/Frame 038424/0044 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 29, 2016
From: DOW STADE PRODUKTIONS GMBH & CO. OHG
To: THE DOW CHEMICAL COMPANY
Reel/Frame 038424/0085 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 29, 2016
From: THE DOW CHEMICAL COMPANY
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 038424/0123 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 29, 2016
From: PIERINI, PETER E.
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 038424/0254 →