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SYNTHESIS AND CHARACTERIZATION OF NEW POLYMERIC MATERIALS BASED ON WATER SOLUBLE STARCH COMPOSITES M.A. ElSheikh*, A. Hebeish, A. Waly, M.H. ElRafie and J.T. Guthrie** National Research Center, Textile Research Division, Dokki, Cairo, Egypt. ** University of Leeds, Colour Chemistry Dept., Leeds, LS2 9JT, UK *Address in UK *Address in Egypt University of Leeds, National Research Center Colour Chemistry Dept. Textile Research division Leeds, LS2 9JT, UK Dokki, Cairo, Egypt Tel.: 00441132332939 Tel.: 002023371211-4960 Fax: 00441132332947 Fax: 002023370931 Email : [email protected]

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SYNTHESIS AND CHARACTERIZATION OF

NEW POLYMERIC MATERIALS BASED ON

WATER SOLUBLE STARCH COMPOSITES

M.A. ElSheikh*, A. Hebeish, A. Waly, M.H.

ElRafie and J.T. Guthrie**

National Research Center, Textile Research

Division, Dokki, Cairo, Egypt.

** University of Leeds, Colour Chemistry Dept.,

Leeds, LS2 9JT, UK

*Address in UK *Address in Egypt

University of Leeds, National Research Center

Colour Chemistry Dept. Textile Research division

Leeds, LS2 9JT, UK Dokki, Cairo, Egypt

Tel.: 00441132332939 Tel.: 002023371211-4960

Fax: 00441132332947 Fax: 002023370931

Email : [email protected]

2

Contents

Part I:

Preparation and Characterization of Carboxymethyl

Starch (CMS)

Part II:

Graft copolymerisation of Acrylic Acid onto

Carboxymethyl Starch Using Chemical Initiation

.......................

Part III:

Graft copolymerisation of Acrylic Acid onto

Carboxymethyl Starch Using Photo Initiation

3

Part1: Preparation and Characterization of

Carboxymethyl Starch (CMS) Introduction

Why CMS

Solubility

Viscosity

wide Application

Experimental

• Materials

• starch

• Native Starch (NS

• Hydrolyzed Starch (

) η= 239 (mPa S)

HS

• Highly Hydrolyzed Starch (

), η=134(mPa S)

HHS

η = 61(mPa S)

),

• NaOH, Na2Co3 , Ethanol (commercial

Grade)

• ClCH2COOH, Laboratory Grade

4

Carboxymethylation

• ClCH2COOH reacts with Na2Co3 to form

ClCH2COONa.

• Starch is stirred with NaOH in Ethanol/Water

mixture.

• Starch [St.-(OH)] reacts with ClCH2COONa in

presence of NaOH to form Carboxymethyl Starch

(CMS).

• 2 ClCH2COOH + Na2CO3 2 ClCH2COONa + H2O+

CO2

• St.-OH + ClCH2COONa + NaOH St-OCH2COONa

+NaCl + H2O

CMS is separated from the liquor by filtration,

washed with 80% Ethanol and dried.

5

Viscosity(η) and Degree of Substitution (DS)

• NS, HS and HHS

• Three concentrations of ClCH2COOH, Na2Co3 and

NaOH, based on theoretical calculations of DS (0.1,

0.3 and 0.5), were used for each Starch sample.

were used to provide CMS with

different viscosity.

• Nine CMS samples were prepared for the study

• Three from NS

• Three from

with theoretical DS of 0.1, 0.3

and 0.5

HS

• Three from

with theoretical DS of 0.1, 0.3

and 0.5

HHS

with theoretical DS of 0.1, 0.3

and 0.5

6

More CMS Samples

• 5 kg. Of CMS from NS with theoretical DS of

0.3 was prepared for further study and

applications symbolized by “

CMS*”

• 1 kg. Of CMS from NS with theoretical DS of

0.5 was prepared for further study and

applications symbolized by “CMS**

7

Analysis and Characterization

In comparison with NS.

All the CMS samples were analyzed to determine:

• Total Carboxyl content (mmole/100g CMS)

• DS

• Viscosity at different shear rates (mPa s)

CMS* and CMS**

• Rheological properties

were analyzed to determine:

• Change in surface structure using SEM

• Thermal behavior using DSC

8

Results and Discussion

• All samples prepared using theoretical DS of 0.1

gave CMS with DS ~ 0.04 regardless the viscosity

of the starch used.

• All samples prepared using theoretical DS of 0.3

gave CMS with DS ~ 0.2 regardless the viscosity of

the starch used.

• All samples prepared using theoretical DS of 0.5

gave CMS with DS ~ 0.4 regardless the viscosity of

the starch used.

• Viscosity of the prepared CMS depends on the

starch used.

9

Characteristics of CMS prepared from starch with different levels of

hydrolysis (NS, HS and HHS

; η = 239, 134 and 61 (mPa s) respectively)

Theoretical

Practical DS

- COOH Content

( mmole/100g CMS)

η

(mPa s)

Solubility

in cold water

NS, HS, HHS NS HS HHS NS HS HHS NS HS HHS NS HS HHS

0.1

0.046 0.044 0.038 28 26.7 23.2 134.2 38.7 10.5 slightly soluble

0.3 0.191 0.199 0.211 110.4 111.8 121.2 169.2 70 18.1 completely

soluble 0.5 0.393 0.388 0.343 210.2 188.6 198.6 198.3 212.3 31.5 completely

soluble

10

Effect of Degree of Substitution of CMS on its Viscosity

0

50

100

150

200

250

0 0.1 0.2 0.3 0.4 0.5DS

Vis

cosi

ty (m

Pa s)

CMS from NS

CMSfrom HS

CMS from HHS

11

Effect of the Degree of Substitution of CMS on its Viscosity measured at Different Rates of

Shear

0

100

200

300

400

500

600

700

800

0 150 300 450 600 750 900 1050 1200 1350Rate of Shear (s-1)

Vis

cosi

ty (m

Pa s)

CMS (DS=0.046, NS)CMS (DS=0.044,HS)CMS (DS=0.038, HHS)CMS (DS=0.191, NS)CMS (DS=0.199,HS)CMS (DS=0.211, HHS)CMS (DS=0.393, NS)CMS (DS=0.388,HS)CMS (DS=0.343, HHS)NSHHS

12

NS, CMS* and Samples Chosen:

CMS**

• NS: DS = 0.0, η=239 (mPa s)

• CMS*: DS= 0.2, η=158 (mPa s), from NS

• CMS**: DS= 0.4, η=198 (mPa s), from NS

13

Characterization

• Rheology

• V1; viscosity on applying mechanical stress

• V2; viscosity on removing mechanical stress

• SEM

• Thermal Analysis (DSC)

14

Effect of the Extent of Carboxymethylation on the Rheological Properties of CMS

0

100

200

300

400

500

600

700

0 200 400 600 800 1000 1200 1400

Rate of Shear (s-1)

Vis

cosi

ty (m

Pa s)

V1 (NS, DS=0.0) V2 (NS, DS= 0.0)V1 (CMS*, DS= 0.2)V2 (CMS*, DS= 0.2)V1 (CMS**, DS= 0.4)V2 (CMS**, DS= 0.4)

15

SEM

a, NS; b, CMS*; and c, CMS**

NS, CMS* and CMS**, Powder Form

16

DSC

a

b

c

a, NS; b, CMS*; c, CMS**

NS, CMS* and CMS**, Powder Form

17

Advantages of the carboxymethylation

process used

• Homogeneous distribution of the reactants.

• No heat of reaction.

• No excess alkali (pH after carboxymethylation~8)

• Replication (same DS at same conditions)

• High reaction efficiency for higher DS

• 0.1 ~ 0.04 (40%)

• 0.3 ~ 0.2 (66.7%)

• 0.5 ~ 0.4 (80%)

• Recycling of Ethanol for purification.

Applications:

• Sizing agents in the paper and textile industries.

• Printing thickeners for pigment dispersions.

• Adhesives.

• Ion exchange materials.

18

Part II: Graft copolymerisation of Acrylic

Acid onto Carboxymethyl Starch Using

Chemical Initiation

Introduction

Aim

Water soluble polymer

High carboxyl content

Industrially applicable

Experimental

• Materials

• CMS, laboratory prepared (Part1)

• Acrylic Acid (AA), Potassium Bromate and

Thiourea dioxide (TUDO) are laboratory

grade.

• Ethanol, commercial grade.

19

Preparation of Poly(acrylic acid)- CMS

• Sample handling

• Grafting

• All used CMS were in the form -COONa

• Cooking

• Cooling to the reaction temperature

• Adding TUDO under continuous stirring

• Adding AA under continuous stirring

• Adding KBrO3 under continuous stirring

• Left for the required time

• Separation of homopolymer

20

• Analysis

• All samples were monitored to Total

Conversion % (TC%) of Acrylic Acid

• Selected samples were monitored to:

• -COOH content (mmole/100g CMS)

• SEM

• Thermal Analysis (DSC)

21

Reaction Mechanism

Here, x (= n-6) is the number of electrons contributed from the reaction medium.

The isothiourea dioxide radicals (I) attack the starch chain to form starch free radicals (II)

(Reaction 3.3)

Furthermore, the isothiourea dioxide radicals can strongly initiate hompolymerisation of the

acrylic acid monomer molecules (Reaction 3.4). Thus:

22

The reaction of starch free radicals with the acrylic acid monomer initiates the grafting reaction

along the starch backbone (Reaction 3.5).

initiation

propagation

(3.5)

23

Results and Discussion

Factors Affecting Total Conversion %

Studied:

• Effect of Material : Liquor ratio.

• Effect of TUDO concentration, mmole/100g

CMS.

• Effect Redox system concentration

mmole/100g CMS.

• Effect of reaction temperature, oC.

• Effect of Acrylic Acid concentration, “%

(OWS)” (% based On Weight of Substrate)

• Effect of DS and viscosity(mPa s) of the used

CMS.

• Reaction time.

24

Effect of M:L Ratio on TC% of Acrylic Acid

0

20

40

60

80

100

0 20 40 60 80 100

Time (min.)

CMS, (DS= 0.199), (η= 70 mPa s); AA, 30%(OWS); Temp., 40oC; [(KBrO3)/(TUDO)],

6/6 mmole/100g CMS.

TC

%

01:0301:0401:0501:06

25

Effect of M:L Ratio on TC% of Acrylic Acid

1:3 1:41:5

1:6

0

20

40

60

80

100

M:L Ratio

CMS, (DS= 0.199), (η= 70 mPa s); AA, 30%(OWS); Temp., 40oC; [(KBrO3)/(TUDO)],

6/6 mmole/100g CMS; Time, 90 min.

TC

%

26

Effect of TUDO Concentration on TC% of Acrylic Acid

0

20

40

60

80

100

0 20 40 60 80 100Time (min.)

CMS, (DS= 0.199), (η= 70 mPa s); AA, 30%(OWS); Temp., 40oC; M:L Ratio, 1:5;

[KBrO3],6 mmole/100g CMS.

TC

%

2 mmole/100g CMS4 mmole/100g CMS6 mmole/100g CMS8 mmole/100g CMS10 mmole/100g CMS

27

Effect of TUDO Concentration on TC% of Acrylic Acid

0

20

40

60

80

100

0 2 4 6 8 10 12[TUDO] mmole/100g CMS

CMS, (DS= 0.199), (η= 70 mPa s); AA, 30%(OWS); Temp., 40oC; M:L Ratio, 1:5; [KBrO3],6 mmol/100g CMS; Time, 90 min.

TC

%

28

Effect of Initiator Concentration [(KBrO3)/(TUDO)] mmole/100g CMS on

TC% of Acrylic Acid

0

20

40

60

80

100

0 20 40 60 80 100

Time (min.)

CMS, (DS= 0.199), (η= 70 mPa s); AA, 30%(OWS); Temp., 40oC; M:L Ratio, 1:5.

TC

%

3/3 mmole/100g CMS4/4 mmole/100g CMS5/5 mmole/100g CMS6/6 mmole/100g CMS7/7 mmole/100g CMS8/8 mmole/100g CMS

29

Effect of Initiator Concentration [(KBrO3)/(TUDO)] mmole/100g CMS on

TC% of Acrylic Acid

3/3 4/4

5/56/6 7/7

8/8

0

20

40

60

80

100

[(KBrO3)/(TUDO)] mmole/100g CMS

CMS, (DS= 0.199), (η= 70 mPa s); AA, 30%(OWS); Temp., 40oC; M:L Ratio, 1:5; Time,

90 min.

TC

%

30

Effect of Temperature on TC% of Acrylic Acid

0

20

40

60

80

100

0 20 40 60 80 100

Time (min.)

CMS, (DS= 0.199), (η= 70 mPa s); AA, 30%(OWS); M:L Ratio, 1:5; [(KBrO3)/(TUDO)],

6/6 mmole/100g CMS.

TC

%

30405060

31

Effect of Temperature on TC% of Acrylic Acid

0

20

40

60

80

100

0 10 20 30 40 50 60 70Temperature (oC)

CMS, (DS= 0.199), (η= 70 mPa s); AA, 30%(OWS); M:L Ratio, 1:5; [(KBrO3)/(TUDO)],

6/6 mmole/100g CMS; Time, 90 min.

TC

%

32

Effect of Acrylic Acid Concentration (% OWS) on TC% of Acrylic Acid

0

20

40

60

80

100

0 20 40 60 80 100Time (min.)

CMS, (DS= 0.199), (η= 70 mPa s); M:L Ratio, 1:5; [(KBrO3)/(TUDO)], 6/6 mmole/100g CMS;

Temp., 40oC.

TC

%

20% (OWS)30% (OWS)40% (OWS)60% (OWS)80%(OWS)

33

Effect of Acrylic Acid Concentration (% OWS) on TC% of Acrylic Acid

0

20

40

60

80

100

0 20 40 60 80 100AA% (OWS)

CMS, (DS= 0.199), (η= 70 mPa s); M:L Ratio, 1:5; [(KBrO3)/(TUDO)], 6/6 mmole/100g CMS;

Temp., 40oC; Time, 90 min.

TC

%

34

Effect of DS and Viscosity (mPa s) of CMS on TC% of Acrylic Acid

0

20

40

60

80

100

0 20 40 60 80 100Time (min.)

M:L Ratio, 1:5; [(KBrO3)/(TUDO)], 6/6 mmole/100g CMS; Temp., 40oC; AA, 30%

(OWS).

TC

%

DS ,Viscosity0.046, 134.20.044, 38.70.038, 10.50.191, 169.20.199, 700.211, 18.10.393, 198.30.388, 212.30.343, 31.5

35

Effect of DS and Viscosity (mPa s) of CMS on TC% of Acrylic Acid

0

20

40

60

80

100

0 0.1 0.2 0.3 0.4 0.5DS

M:L Ratio, 1:5; [(KBrO3)/(TUDO)], 6/6 mmole/100g CMS; Temp., 40oC; AA, 30%

(OWS); Time, 90 min.

TC

%

CMS from NS

CMS from HS

CMS from HHS

36

Optimum conditions: • Material: Liquor Ratio, 1:5

• Equimoleculare Ratio of KBrO3/TUDO, 6/6

mmole/100g CMS.

• Reaction Temperature, 40oC.

• Acrylic Acid, 30% (OWS).

• CMS prepared from HS with DS= 0.199 and

η=70 mPa s. • Reaction time, 90 min.

Chosen Sample Sample prepared by applying the optimum

conditions on CMS from NS [DS, 0.2; COOH

content, (115 mmole/100g CMS); η, (158 mPa s)] was

chosen for characterization.

37

Characterization

-COOH Content: It was found out that -COOH content due to grafting

is very little (87 mmole/100g CMS), less than COOH

content due to carboxymethylation (115 mmole/100g

CMS).

38

SEM CMS*-PAA

39

Thermal Analysis (DSC) CMS*-PAA

40

Advantages of the polymerization process

used:

• High viscosity of the composite.

• High adhesion of the composite.

• High Swelling in water of the dry composite or dry

graft copolymer.

• Water soluble composite.

Disadvantages of the polymerization process

used:

• Little graft yield.

• High homopolymer yield.

41

Conclusion

• The process could be recommended for providing a

water soluble starch composite.

• The process could not be not recommended for

providing a CMS-PAA graft copolymer.

Advice In case of having CMS-PAA graft copolymer with

high graft yield, other initiation system should be

used. (See Part III)

Applications: • Sizing agents in the paper and textile industries.

• Printing thickeners for pigment dispersions.

• Adhesives.

• Ion exchange materials.

42

Acknowledgments

• Egyptian Government for funding the research at

Leeds University.

• Egyptian Government for providing funds for

attendance at American Chemical Society Meeting

in San Francisco.

• Professors in National Research Center (NRC),

Textile Research Division (TRD) and University of

Leeds, Colour Chemistry Dept. for supervision:

Prof. Dr. A. Hebeish (NRC, TRD)

Prof. Dr. A. Waly (NRC, TRD)

Prof. Dr. M.H. ElRafie (NRC,TRD)

Prof. Dr. J.T. Guthrie (University of Leeds, Colour

Chemistry Dept.)