WO2004106415A2 - Carboxymethylcellulose having improved solubility in water - Google Patents

Carboxymethylcellulose having improved solubility in water Download PDF

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Publication number
WO2004106415A2
WO2004106415A2 PCT/EP2004/050964 EP2004050964W WO2004106415A2 WO 2004106415 A2 WO2004106415 A2 WO 2004106415A2 EP 2004050964 W EP2004050964 W EP 2004050964W WO 2004106415 A2 WO2004106415 A2 WO 2004106415A2
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WIPO (PCT)
Prior art keywords
carboxymethylcellulose
powder
rpm
granulation
procedure
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PCT/EP2004/050964
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French (fr)
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WO2004106415A3 (en
Inventor
Cristina Demarchi
Giuseppe Li Bassi
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Lamberti Spa
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Publication date
Application filed by Lamberti Spa filed Critical Lamberti Spa
Priority to DE602004002592T priority Critical patent/DE602004002592D1/en
Priority to EP04741680A priority patent/EP1629030B1/en
Priority to BRPI0410855-8A priority patent/BRPI0410855A/en
Publication of WO2004106415A2 publication Critical patent/WO2004106415A2/en
Publication of WO2004106415A3 publication Critical patent/WO2004106415A3/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/12Powdering or granulating
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B11/00Preparation of cellulose ethers
    • C08B11/20Post-etherification treatments of chemical or physical type, e.g. mixed etherification in two steps, including purification
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2301/00Characterised by the use of cellulose, modified cellulose or cellulose derivatives
    • C08J2301/08Cellulose derivatives
    • C08J2301/26Cellulose ethers
    • C08J2301/28Alkyl ethers

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Medicinal Preparation (AREA)
  • Jellies, Jams, And Syrups (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

The present invention relates to a procedure for the preparation of granulated ca rboxymethylcellulose which dissolves rapidly in water; the procedure consists in granulating carboxymethylcellulose in the form of powder in the presence of an aqueous solution of low viscosity carboxymethylcellulose.

Description

Description
FAST DISSOLVING CARBOXYMETHYLCELLULOSE .
[0001] The present invention relates to a procedure for the preparation of granulated carboxymethylcellulose which dissolves rapidly in water.
[0002] Carboxymethylcellulose is usually commercialised in the form of powder and used as thickener in numerous water based formulations.
[0003] It is well known that many problems are encountered while dissolving water soluble polysaccharides.
[0004] The formation of lumps is one of these problems, because lumps strongly increase the time needed to reach the maximum viscosity of the solution.
[0005] Another problem is the generation of foams, which is due to the incorporation of large amount of air in the solution.
[0006] To solve these problems it is necessary to adopt technical devices, such as heating the water, conducting the dissolution at reduced pressure, choosing particular stirring facilities; all this, causes practical difficulties and increases the overall operation costs.
[0007] The presence of fine powders in the air is another problem connected with the dissolution in water of polysaccharides.
[0008] In US 6,294,665 (FUJI OIL CO., LTD) a procedure especially directed to the solution of the above cited problems is described; the procedure is based on the use of a solution comprising an emulsifier, among other essential constituents.
[0009] It has now been found, and it constitutes a fundamental object of the present invention, that it is possible to obtain a granulated carboxymethylcellulose which rapidly dissolves in water, by granulating carboxymethylcellulose in the form of powder in admixture with an aqueous solution of low viscosity carboxymethylcellulose.
[0010] In the present text, with the expression "carboxymethylcellulose in the form of powder" we mean carboxymethylcellulose having particle size of at least 90 wt% (percent by weight) finer than 1 mm; with the expression "low viscosity carboxymethylcellulose" we mean carboxymethylcellulose having Brookfield viscosity comprised between 1 ,000 and 6,000 mPa*s at 25 wt% and 20 rpm. [0011] Surprisingly, the admixture of carboxymethylcellulose in the form of powder and of the aqueous solution of low viscosity carboxymethylcellulose according to the invention eliminates the necessity of using an emulsifier in the granulating step. [0012] This feature is very advantageous, because the presence of undesired substances (emulsifiers) in the finished product is thereby avoided. [0013] The granulated carboxymethylcellulose of the invention, beside being fast dissolvable in water, does not lead to the formation of lumps and foams, when dissolved, and of dusting, when handled. [0014] According to a fundamental aspect of the present invention, the low viscosity carboxymethylcellulose, which is used in the form of an aqueous solution in the granulation, has Brookfield viscosity comprised between
1,000 and 6,000 mPa*s, preferably between 3,000 and 4,000 mPa*s at 25 wt% and 20 rpm. [0015] According to another fundamental aspect of the invention, the aqueous solution of low viscosity carboxymethylcellulose used in the granulation contains from 5 to 20 wt% of low viscosity carboxymethylcellulose, preferably from 10 to 15 wt%. [0016] For the realisation of the present invention, the weight ratio between the carboxymethylcellulose in the form of powder and the aqueous solution of low viscosity carboxymethylcellulose is comprised between 3.0 and 5, preferably between 3.2 and 4.5. [0017] The carboxymethylcellulose in the form of powder to be granulated has a substitution degree (DS) comprised between 0.4 and 1.2 and Brookfield viscosity comprised between 30 and 30,000 mPa*s at 2 wt% and 60 rpm. [0018] The carboxymethylcellulose in the form of powder that can be utilised in the procedure according to the invention has a maximum water content of
10 wt%. [0019] The granulating methods utilisable to obtain the fast dissolving granulated carboxymethylcellulose are those commonly in use in this field; in particular, the carboxymethylcellulose in the form of powder can be granulated by means of a fluidised bed, a rolling, a spray drying or a stirring granulating method. [0020] Preferably, the granulation of carboxymethylcellulose in the form of powder according to the invention is performed by means of a rolling granulating apparatus having a stirring speed comprised between 200 and 300 rpm.
[0021 ] Another advantage of the procedure of the invention is the fact that the granules of carboxymethylcellulose obtained have a regular structure, and are accompanied by a very low percentage of non-granulated fine powder.
[0022] As a conclusion, the use of the procedure for the granulation of carboxymethylcellulose according to the invention, allows to shorten the dissolution time of the granulated carboxymethylcellulose and to avoid the formation of foams and dusting during operations.
[0023] The following examples illustrate embodiments of the invention and are not intended to unduly limit the invention itself.
[0024] Example 1.
[0025] 100 parts by weight of carboxymethylcellulose in the form of powder (DS= 0.6 and Brookfield viscosity of 52 mPa*s at 2 wt% and 60 rpm) are granulated with a rolling granulating apparatus (rotating speed 250 rpm) with 30 parts by weight of a 12.5 wt% aqueous solution of carboxymethylcellulose (DS= 0.6 and Brookfield viscosity of 3,200 mPa*s at 25 wt% and 20 rpm), the aqueous solution having Brookfield viscosity of 86 mPa*s at 60 rpm.
[0026] Example 2.
[0027] 100 parts by weight of carboxymethylcellulose in the form of powder (DS= 1.0 and Brookfield viscosity of 6,220 mPa*s at 2 wt% and 60 rpm) are granulated with a rolling granulating apparatus (rotating speed 250 rpm) with 27 parts by weight of a 12.5 wt% aqueous solution of carboxymethylcellulose (DS= 0.6 and Brookfield viscosity of 3,100 mPa*s at 25 wt% and 20 rpm), the aqueous solution having Brookfield viscosity of 73 mPa*s at 60 rpm.
[0028] Example 3.
[0029] 100 parts by weight of carboxymethylcellulose in the form of powder (DS= 0.8 and Brookfield viscosity of 906 mPa*s at 2 wt% and 60 rpm) are granulated with a rolling granulating apparatus (rotating speed 275 rpm) with 25 parts by weight of a 12.5 wt% aqueous solution) of carboxymethylcellulose (DS= 0.6 and Brookfield viscosity of 3,900 mPa*s at 25 wt% and 20 rpm), the aqueous solution having Brookfield viscosity of
102 mPa*s at 60 rpm.
[0030] Testing dissolution time, formation of lumps and foams.
[0031] 350 ml of demineralised water are poured in a 500 ml becker, and 2.5 g of granulated carboxymethylcellulose are added.
[0032] The mixture is slowly stirred with a magnetic stirrer, visually determining the time when complete dissolution is reached and verifying the occasional presence of foams.
[0033] The presence of lumps is determined by filtering the solution with a 2 mm sieve.
[0034] Testing dusting behaviour. [0035] 100 g of granulated carboxymethylcellulose are placed in a 1 1 transparent jar; the jar is capped and repeatedly turned upside down during 15 seconds. The jar is then allowed to stand still and immediately the presence of dusting inside the jar is observed.
[0036] Testing particle-size. [0037] The particle-size testing is made by sieving . [0038] In the following tables (Table 1 and Table 2), the essential features of the examples and the results of the tests are respectively reported.
[0039]
Table 1
Figure imgf000005_0001
[0040] VCMC = Brookfield viscosity of the carboxymethylcellulose in the form of powder, in mPa*s (60 rpm, 2 wt%) . [0041] Go Particle-size of the carboxymethylcellulose in the form of powder (wt% of particles from 1 to 0.355 mm) [0042] DSCMC = Degree of substitution of the carboxymethylcellulose in the form of powder [0043] VcMCsol = Brookfield viscosity of the low viscosity carboxymethylcellulose, in mPa*s (20 rpm, 25 wt%).
[0044] Vsoi = Brookfield viscosity of the 12.5 wt% aqueous solution of low viscosity carboxymethylcellulose
[0045] DSC CSOI = Degree of substitution of the low viscosity carboxymethylcellulose
[0046] PcMc/ sor Weight ratio between the carboxymethylcellulose in the form of powder and the aqueous solution of low viscosity carboxymethylcellulose.
[0047]
Table 2
Figure imgf000006_0001
[0048] T iss. = Dissolution time in minutes
[0049] G = Particle-size of the granulated carboxymethylcellulose (wt% of particles from 1 to 0.355 mm)

Claims

Claims
1. Procedure for the granulation of carboxymethylcellulose in the form of powder having a degree of substitution (DS) comprised between 0.4 and 1.2 and Brookfield viscosity comprised between 30 and 30,000 mPa*s at 2 wt% and 60 rpm, characterised by the fact that the granulation is performed by mixing the carboxymetylcellulose in the form of powder with an aqueous solution containing from 5 to 20 wt% of low viscosity carboxymetylcellulose having Brookfield viscosity comprised between 1 ,000 and 6,000 mPa*s at 25 wt% and 20 rpm, the weight ratio between the carboxymethylcellulose in the form of powder and the aqueous solution of low viscosity carboxymethylcellulose being comprised between 3.0 and 5.
2. Procedure for the granulation of carboxymethylcellulose in the form of powder according to claim 1., wherein the low viscosity carboxymethylcellulose has Brookfield viscosity comprised between 3,000 and 4,000 mPa*s at 25 wt% and 20 rpm.
3. Procedure for the granulation of carboxymethylcellulose in the form of powder according to claim 2., wherein the aqueous solution contains from 10 to 15 wt% of low viscosity carboxymethylcellulose.
4. Procedure for the granulation of carboxymethylcellulose in the form of powder according to claim 3., wherein the weight ratio between the carboxymethylcellulose in the form of powder and the aqueous solution of low viscosity carboxymethylcellulose is comprised between 3.2 and 4.5.
5. Procedure for the granulation of carboxymethylcellulose in the form of powder according to claim 4., wherein the carboxymethylcellulose in the form of powder has a maximum water content of 10 wt%.
6. Procedure for the granulation of carboxymethylcellulose in the form of powder according to claim 5., wherein the granulation is performed by means of a rolling granulating apparatus.
PCT/EP2004/050964 2003-06-03 2004-06-01 Carboxymethylcellulose having improved solubility in water WO2004106415A2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
DE602004002592T DE602004002592D1 (en) 2003-06-03 2004-06-01 CARBOXYMETHYL CELLULOSE WITH IMPROVED SOLUBILITY IN THE WATER
EP04741680A EP1629030B1 (en) 2003-06-03 2004-06-01 Carboxymethylcellulose having improved solubility in water
BRPI0410855-8A BRPI0410855A (en) 2003-06-03 2004-06-01 procedure for granulation of carboxymethylcellulose in powder form

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ITVA2003A000017 2003-06-03
IT000017A ITVA20030017A1 (en) 2003-06-03 2003-06-03 CARBOXYMETHYLCELLULOSE AT HIGH SPEED DISSOLUTION IN WATER.

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WO2004106415A2 true WO2004106415A2 (en) 2004-12-09
WO2004106415A3 WO2004106415A3 (en) 2005-03-17

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EP (1) EP1629030B1 (en)
AT (1) ATE340821T1 (en)
BR (1) BRPI0410855A (en)
DE (1) DE602004002592D1 (en)
IT (1) ITVA20030017A1 (en)
WO (1) WO2004106415A2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010117783A1 (en) * 2009-03-31 2010-10-14 Dow Global Technologies Inc. Tartaric salt stabilizer for wine
CN112608388A (en) * 2020-12-28 2021-04-06 浙江圣兆药物科技股份有限公司 Refining method of sodium carboxymethylcellulose for injection

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4507473A (en) * 1983-03-09 1985-03-26 Wolff Walsrode Aktiengesellschaft Process for the continuous granulation of carboxymethyl cellulose

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5936940B2 (en) * 1976-10-05 1984-09-06 ダイセル化学工業株式会社 Granulation method of carboxymethylcellulose sodium salt
JPH082967B2 (en) * 1992-06-05 1996-01-17 日本製紙株式会社 Granulation method of water-soluble cellulose derivative

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4507473A (en) * 1983-03-09 1985-03-26 Wolff Walsrode Aktiengesellschaft Process for the continuous granulation of carboxymethyl cellulose

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN vol. 0020, no. 85 (C-017), 12 July 1978 (1978-07-12) -& JP 53 045357 A (DAICEL CHEM IND LTD), 24 April 1978 (1978-04-24) -& DATABASE CHEMABS [Online] CHEMICAL ABSTRACTS SERVICE, COLUMBUS, OHIO, US; 1984, XP002298338 retrieved from STN Database accession no. 1978:460679 *
PATENT ABSTRACTS OF JAPAN vol. 0183, no. 17 (M-1622), 16 June 1994 (1994-06-16) & JP 6 071643 A (NIPPON PAPER IND CO LTD), 15 March 1994 (1994-03-15) *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010117783A1 (en) * 2009-03-31 2010-10-14 Dow Global Technologies Inc. Tartaric salt stabilizer for wine
CN102356119A (en) * 2009-03-31 2012-02-15 陶氏环球技术有限责任公司 Tartaric salt stabilizer for wine
AU2010234846B2 (en) * 2009-03-31 2014-10-30 Dow Global Technologies Llc. Tartaric salt stabilizer for wine
CN112608388A (en) * 2020-12-28 2021-04-06 浙江圣兆药物科技股份有限公司 Refining method of sodium carboxymethylcellulose for injection

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WO2004106415A3 (en) 2005-03-17
BRPI0410855A (en) 2006-07-04
DE602004002592D1 (en) 2006-11-09
ITVA20030017A1 (en) 2004-12-04
EP1629030B1 (en) 2006-09-27
EP1629030A2 (en) 2006-03-01
ATE340821T1 (en) 2006-10-15

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