Process for the production of a rheology modifier containing composition

Patent metadata

Field	Value
Publication number	US-2016130536-A1
Application number	US-201614996724-A
Country	US
Kind code	A1
Filing date	Jan 15, 2016
Priority date	Jul 27, 2011
Publication date	May 12, 2016
Grant date	—

Abstract

A process for the production of a rheology modifier containing composition comprising the steps of: providing a rheology modifier, wherein said rheology modifier is selected from the group consisting of a water swellable polymer, a non-water soluble crystalline polymer, and mixtures thereof; providing a substantially anhydrous water-miscible liquid carrier; and dispersing said rheology modifier in said substantially anhydrous water-miscible liquid carrier to generate a slurry having a viscosity of less than 2000 mPas at 0.1 s −1 and 20° C. when measured using an AR 1000 rheometer.

First claim

What is claimed is:

1 . A process for the production of a rheology modifier containing composition comprising the steps of:
(a) first, providing a rheology modifier, wherein said rheology modifier is selected from the group consisting of a water swellable polymer, a non-water soluble crystalline polymer, and mixtures thereof; (b) providing a substantially anhydrous water-miscible liquid carrier; and (c) second, dispersing said rheology modifier into said substantially anhydrous water-miscible liquid carrier to generate a slurry having a viscosity of less than 2000 mPas at 0.1 s −1 and 20° C. when measured using an AR 1000 rheometer prior to any mixing with water.

2 . A process according to claim 1 wherein said slurry has a viscosity of less than 1000 mPas, measured at 0.1 s −1 and 20° C.

3 . A process according to claim 1 wherein said slurry has a viscosity of less than 250 mPas, measured at 0.1 s −1 and 20° C.

4 . A process according to claim 1 wherein said water swellable polymer is selected from the group consisting of polyacrylates, polymethacrylates, polyacrylamides, polymethacrylamides, polyurethanes and co-polymers thereof, polysaccharides, cellulose ethers, gums, and mixtures thereof.

5 . A process according to claim 1 wherein said water swellable polymer is selected from the group consisting of cellulose ethers, gums, and mixtures thereof.

6 . A process according to claim 1 wherein said water swellable polymer is a gum selected from the group consisting of guar gum, xanthan gum, gellan gum and mixtures thereof.

7 . A process according to claim 1 wherein said non-water soluble crystalline polymer is micro fibril cellulose.

8 . A process according to claim 1 wherein said non-water soluble crystalline polymer is micro fibril cellulose and wherein said micro fibril cellulose is combined with a carboxymethylcellulose, a modified carboxymethylcellulose, a quaternized polysaccharide, and mixtures thereof; and optionally, a polymeric thickener selected from xanthum products, pectin, alginates, gellan gum, welan gum, diutan gum, rhamsan gum, carrageenan, guar gum, agar, gum arabic, gum ghatti, karaya gum, gum tragacanth, tamarind gum, locust bean gum, and mixtures thereof.

9 . A process according to claim lwherein said substantially anhydrous water-miscible liquid carrier is selected from the group consisting of surfactants, humectants, polymers, oils, and mixtures thereof.

10 . A process according to claim 1 wherein said substantially anhydrous water-miscible liquid carrier consists essentially of a nonionic surfactant.

11 . A process according to claim 1 wherein said substantially anhydrous water-miscible liquid consists essentially of a nonionic surfactant selected from alcohol alkoxylates with a hydrophilic-lipophilic balance of greater than 10.

12 . A process according to claim 1 wherein said slurry comprises less than 3% of air.

13 . A process according to claim 1 wherein said slurry comprises less than 0.1% of air.

14 . A process according to claim 1 wherein step (c) comprises the step of providing a polyvalent salt and mixing said salt with said rheology modifier and said substantially anhydrous water-miscible liquid carrier.

15 . A process according to claim 1 wherein step (c) comprises the step of providing a tri-valent citrate, and mixing said citrate with said rheology modifier and said substantially anhydrous water-miscible liquid carrier.

16 . A process according to claim 1 wherein following step (c), the slurry is mixed with remaining ingredients to generate a final composition and wherein said rheology modifier consists of micro fibril cellulose, and wherein said micro fibril cellulose is activated substantially simultaneously, or after, mixing with remaining ingredients to generate a final composition.

17 . A process according to claim 1 wherein following step (c), the slurry is mixed with a solvent to generate a premix, step (d) and wherein said rheology modifier consists of micro fibril cellulose and wherein said micro fibril cellulose is activated substantially simultaneously, or after, mixing with said solvent, optionally said premix containing activated micro fibril cellulose is mixed with remaining ingredients to generate a final composition.

18 . A process according to claim 1 wherein following step (c), the slurry is mixed with water to generate a premix, step (d) in an in-line process and wherein said rheology modifier consists of micro fibril cellulose and wherein said micro fibril cellulose is activated substantially simultaneously, or after, mixing with water, optionally said premix containing activated micro fibril cellulose is mixed with remaining ingredients to generate a final composition.

19 . A process according to claim 1 wherein said slurry is generated in a batch process.

20 . A process for the production of a rheology modifier containing composition comprising the steps of:
(a) first, providing a rheology modifier, wherein said rheology modifier consists of micro fibril cellulose; (b) providing a substantially anhydrous water-miscible liquid carrier; (c) second, dispersing said rheology modifier into said substantially anhydrous water-miscible liquid carrier to generate a slurry having a viscosity of less than 2000 mPas at 0.1 s −1 and 20° C. when measured using an AR 1000 rheometer prior to any mixing with water; and (d) following step (c) said slurry is mixed with water to generate a premix in an in-line process and wherein said micro fibril cellulose is activated substantially simultaneously, or after, mixing with said solvent and said premix containing activated micro fibril cellulose is mixed with remaining ingredients to generate a final composition.

Assignees

• Procter & Gamble

Inventors

• Jones Christopher Stephen
• Yaldizkaya Nuray
• Pinna Raffaele
• Tideman Jeroen
• Keuleers Robby Renilde-Francois

Classifications

• C11D3/222

  Natural or synthetic polysaccharides, e.g. cellulose, starch, gum, alginic acid or cyclodextrin · CPC title

• C11D3/3765

  in liquid compositions · CPC title

• C11D3/3773

  in liquid compositions · CPC title

• C11D17/0004 Primary

  Non aqueous liquid compositions comprising insoluble particles · CPC title

• C11D3/225

  etherified, e.g. CMC · CPC title