Chapter 1 Industrial gums– polysaccharides and their derivatives

1-1 Introduction 1-2 Definition of gums 1-3 Industrially valuable properties of gums 1-4 Modified gums 1-5 Nutritional characteristics of gums 1-6 Method for dissolving gums 1-7 Gelation of gums

1-1 Introduction Industrial gums, which for the most part water-soluble

polysaccharides, have enormously large and broad application in both food and non-food industries

Polysaccharides are used in the food industry because they are wildly available, usually of low cost, and nontoxic

Gums commonly used in foods Starch, cellulose derivatives, guar gum, locust bean gum, pe

ctin, algin, carrageenan, xanthan and gum arabic

1-1 Introduction Gums seldom constitute an entire finished product but

are used most often as additives to improve or control the properties of a food product

The principal property of polysaccharide gums is their easy hydration to produce aqueous solutions possessing high viscosities at low gum concentration

Each gum has special properties that are a result of its individual unique molecular structure

1-2 Definition of gums The Gum refers to plant or microbial polysacc

harides or their derivatives that are dispersible in either cold or hot water to produce viscous mixtures or solutions

Types of gums Exudate gums Seaweed gums Seed gums Microbial gums Starch and cellulose derivatives

1-3 Industrially valuable properties of gums Organoleptic improvements Most essentially linear polysaccharides have a tenden

cy to form helical structure It is important to recognize that a linear glycan will pr

oduce much more viscous solutions than will a branched gluycan of the same number of units, particularly a bush-shape one.

All linear neutral homoglycans have an inherent tendency to associate, to produce a crystalization of the long and unwidely chains

1-3 Industrially valuable properties of gums Linear molecules join to form an association of

segments -- junction zones The ionized linear molecules will not associate

because of the repulsion Change the pH to obtain neutral molecules that will

associate and form a gel or will precipitate from solution

Gel formation and syneresis

Relation of rheological behavior of gum solutions to organoleptic properties

Perception of consistency in food products depends almost entirely on shearing stress that is perceived in the mouth

The shearing force is in the region of 50/sec (rpm)

1-4 Modified gums It is useful for altering chemical and physical

properties to give the polysaccharide new application DS 0.01-0.04 is sufficient

3-4-1 Introduction of neutral groups 3-4-2 Introduction of acidic groups 3-4-3 Introduction of basic groups

1-4-1 Introduction of neutral groups Placement of neutral groups on linear polysaccharides leads

to increased solution viscosity and stability Solubility characteristics are enhanced more by use a hydro

xylated substituent groups than by completely hydrophobic groups

Water solubility diminishes and solubility in organic solvents increases as hydrophobic groups are introduced beyond a DS of about 1.0

Random introduction of substituent groups to a DS of 0.5-1.5 will produce sufficient irregularity in a linear polysaccharide Decrease of junction zone Increase of solubility

1-4-2 Introduction of acidic groups Carboxyl groups may be introduced into a neut

ral polysaccharides by oxidation Sulfation and phosphorylation are commerciall

y useful means for the introduction of strongly ionized groups

Polysaccharide molecules with such groups readily dissolve to form viscous solutions

1-4-3 Introduction of basic groups It is quite easy to derivatize a polysaccharide w

ith a group that contained amino groups To react an ester of a carboxylated polysacchar

ide with ammonia to form the amide

1-5 Nutritional characteristics of gums

Supply caloric requirement Starch : 85% of the world caloric intake 7% of human energy is derived from sugars split from polys

accharides and by metabolic products of microorganisms in the large intestine

Lower transit time and improve intestinal health Lower cholesterol Innocuous and mainly nonmetabolizable dietary comp

onents

1-6 Method for dissolving gums How to prevent partial gelation and forming fish eyes

Add the dry powder gums to a highly turbulent stream of water

Thoroughly mix the gum with a rapidly dissolving material such as sucrose

It is best to dissolve the gum first in water and subsequently add other food components, or to dissolve other soluble components in a separate portion of water for later mixing of the two solutions

1-7 Gelation of gums 1-7-1 Interactions between polysaccharides 1-7-2 Aggregated ordered ribbon conformation in gels

Cation-mediated gelation of alginate Cation-mediated gelation of pectin High-sugar pectin gels Low water activity gels of neutral polysaccharides

1-7-3 Multiple helices in gels Carrageenans gels , Agar gels, Amylose gels 1-3 beta-D-glucan

1-7-4 Mixed polysaccharide interaction

1-7-1 Interactions between polysaccharides Cation-mediated Low-water activity mediate Freeze-thaw-mediate Helical junction zones

1-7-2 Aggregated ordered ribbon conformation in gels

Cation-mediated gelation of alginate Cation-mediated gelation of pectin High-sugar pectin gels Low water activity gels of neutral polysaccharid

es

Cation-mediated gelation of alginate

(14)--D-mannuronate (14)--L-guluronate

Cation-mediated gelation of alginate

Cation-mediated gelation of pectin

(14)--D-galaturonate

High-sugar pectin gels High-methoxyl pectin gelation requires sucrose concen

tration in excess of 65% Solvent-polymer interactions are reduced and polymer

chain-chain associations are favored It is not sufficient to result in gel formation because of

charge-charge repulsions between pectin molecules Charge is overcome by lowering the pH to less than 4.

0, which suppresses the ionization of the -COOH

Low water activity gels of neutral polysaccharides

Repeating unit structure of tamarind (羅望子 )gum

Here about 70% are substituted

Ability to form gel in wide pH range

Maxi.gel strength: 65-72% sucrose

Low water activity gels of neutral polysaccharides

Locust bean gum : overall Mannose: Galactose = 3.5

The least substituted molecules show the greatest tendency to associate and precipitate

M:G = 3.0, cold-water-soluble fractions

M:G = 4.0, hot-water-soluble fractions

Freeze-induced gelation of galactomannans

1-7-3 Multiple helices in gels Double helix: Carrageen

ans gels , Agar gels, Amylose gels

Triple helix: 1-3 beta-D-glucan

Chapter 2 Pectin 2-1 Structure and Terminology 2-2 Production 2-3 Characterization of pectin gel 2-4 Factors affecting gelation 2-5 Chemical properties 2-6 Pectic enzymes 2-7 Structure and mechanisms of gel formation 2-8 Application

2-1 Structure and Terminology

Pectin is heterogeneous complex polysaccharide Its composition varies with the source and the conditio

ns applied during isolation All pectin molecules contain linear segments of (1

4)-linked -D-galactopyranosyluronic acid with some of the carboxyl groups esterified with methanol.

Some of the hydroxyl groups of the galacturonosyl unit (O-2 and O-3) are esterified with acetic acid.

Pectin molecule with methyl esterified or nonesterified carboxyl groups

Amidated pectin has commercial importance

Terminology Protopectin Pectinic acids Pectic acids Pectins

Degree of esterification (DE) > 50 High-methoxyl pectins (HM-pectins) High concentration of soluble solids, low pH

DE < 50 LM-pectins Divalent cations

2-2 Production 1-2-1 Raw materials

Citrus peel (20-30%), apple pomace(10-15%) Sugarbeet waste, sunflower heads, mango waste

Sugarbeet pectin is inferior to citrus or apple pectin Presence of acetate esterification A relatively low molecular mass Presence of large amount of neutral sugar side chain

2-2-2 Extration, Purification, Modification

Two general processes1. Separating the pectin from most other water-soluble

material by precipitation with an alcohol

2.Precipitating pectin as an insoluble salt with suitable multivalent metal ions

2-2-2 Extration, Purification, Modification Extraction: 5

0-90 , pH 1-3, Time 0.5-24h

2-2-3 Standardization Uncontrolled variations in the raw materials will affect their f

unctional properties. Reproducible performance from batch to batch of the final pr

oducts is a must. Unstandardized HM-pectins are usually ‘diluted’ to a uniform

pectin grade (150 grade USA-SAG) The grade USA-SAG is the number of parts of sucrose which,

under standard conditions, can be turn into a gel of standard gel strength by one part of the pectin.

Standard conditions: refractometer soluble solids, 65%; pH 2.20-2.40; gel strength, 23.5% SAG in 2 min measured by Cox and Higby (1944)

2-3 Characterization of pectin gel 2-3-1 gel strength and breaking strength

Some methods measure the gel strength within the elastic limits of the gel

Other methods measure breaking strength

SAG determination method The gel to be tested is prepared in a glass of

standardized dimensions After curing, the gel is carefully removed from

the glass and allowed to stand without support The height of the gel deformation by its own

weight is measured after a specified time % SAG = 100 x (loss of height/original height)

Plunger methods Strain is applied to the gel by means of a plunger---

compression strain Corresponding values of deformation are measured Strain-versus-distance curve can be obtained while the

plunger is forced into the gel at a constant speed Plunger methods are well suited for use in the jam and

jelly industry

2-3-2 Gelling time and temperature Commercial high-ester pectins are usually stand

ardized to a certain gelling time or temperature under specified conditions

Gelation of high-ester pectins may begin later than instant when the gelling system was colled below the gelling temperature

Gelling time is often measured rather than the gelling temperature

Gelling time measurement The test gel is prepared in exactly the same way

as for the SAG determination The still liquid preparation is adjusted to 95 and pou

red into a standard glass in a 30 water bath The setting time is then taken as the time span from

the filling until visual signs of gelation appear Setting time values are 50 sec for commercial ‘rapi

d-set’ pectins and 225 sec for ‘slow-set’ pectins

2-3-3 Factors affecting gelation Temperature Concentration of pectin pH Concentration of cosolutes Concentration of ions Molecular weight Degree of esterification Degree of amidation Presence of acetyl groups Heterogeneity and presence of neutral sugar residues

Temperature A pectin gel is in most cases prepared hot and then solidifie

d by cooling When cooled below the gelation temperature , systems cont

aining LM-pectin will gel almost instantaneously whereas HM-pectin systems will gel after a time lag. HM-pectin gel cannot be remelted LM-pectin gel is thermoreversible

It is often desirable to fill commercial containers at a temperature close to the gelation temperature to prevent flotation of particles (berries)

Concentration of pectin Typical concentrations of pectin in jams and jellies ran

ge from 0.3% to 0.7% 0.3% HM-pectin gelling at about 65% soluble solids 0.7% amidated LM-pectin gelling at about 35% SS

The pectin concentration used is inversely related to the concentration of soluble solids

At fixed levels of all other parameters, increasing the amount of pectin causes the gel strength of the resulting gel to increase.

pH A pH of about 3.0-3.1 is typical for high-sugar jams (H

M-pectin, 65% SS) Low-sugar jams may be slightly less acidic for taste re

asons. (pH 3.1-5.5) Low pH values tent to increase the strength of both H

M- and LM-pectin gels Gels will generally not form above about pH 3.5 in the

case of HM-pectin and about pH 6.5 in the case of LM-pectin

HM-pectin: lower DE need lower pH for gelation

Concentration of cosolutes HM-pectins will gel only in the presence of large conc

entration of materials that lower water concentration /activity The soluble solids must be at least 55% (w/w) Increasing the soluble solids content causes the gelation tem

p. and the gel strength of the resulting gel to increase LM-pectins may be gelled at zero soluble solids, but in

creasing the soluble solids will also positively affect the gelation temp. and gel strength

Concentration of ions Gelation of LM-pectin will only happen in the presenc

e of divalent cations Except for pectates or very low ester pectins which may for

m gels with K inos under certain conditions Most divalent cations may be effective, but only Ca2+ is use

d in food application Increasing Ca2+ concentration results in increasing gel stren

gth and gelling temp. Divalent cations are not necessary for the formation of

an HM-pectin gel

Molecular weight Gels made from either LM or HM-pectin with h

igh molecular weights will be stronger than gels made with pectins of lower molecular weights

Degree of esterification DE values for commercial LM-pectins range from 20-4

0% Those with the lowest DE-values show the highest gelling te

mperatures and the highest sensitivity to Ca2+ In contrast, the highest gelling temp. and the fastest gel

ation of HM-pectins are found with those that have the higest DE Rapid-set (70-75% DE) > medium-rapid-set (65-70% DE) >

Slow-set (55-65% DE) Gel strength: Slow-set + lower pH = rapid-set Gel strength: R > M > S (at same pH)

Degree of amidation (DA) Most commercial LM-pectins are amidation DA values range from 15-20% Amidation causes the pectin to gel at higher tem

p. compared to a nonamidated pectin under the same conditions, and less Ca2+ is needed

Amidation has a positive effect on gel strength

Presence of acetyl groups If some of the galaturonic acid subunits contain

acetyl group at O-2 or O-3, gelation will be hampered Every eight units is esterified this way

The presence of acetyl esters may be a drawback to suggested alternative source of pectin such as sugar beet pulp and sunflower heads

Heterogeneity and presence of neutral sugar residues Two pectin batches may behave differently, even if the

y are similar with respect to molecular weight and DE The distrubution of esterified and free carboxyl groups

has received much attention because it is different in enzymicly deesterified pectins than it is in acid or alkali deesterified pectins. Gel strength: enzymicly deesterified pectins < acid or alkali

deesterified pectins Heterogeneity has been reported to be advantageous to

the gel-forming ability of a pectin

Heterogeneity and presence of neutral sugar residues

The rhamnose content has impact on the flexibility of the molecules (rhamonse insertions in the backbone)

The side chains of neutral sugar may sterically hinder gelation or limit the size of junction zone

2-5 Chemical properties Pectins are polyanions at neutral pH and approa

ch zero charge at low pH Dissociations of the individual –COOH groups

are not independent: pK = 2.9-3.3 The pH at 50% dissociation of the pectin ranges fro

m 3.5 through 4.5 React with positively charged polymers, such as pro

tein at pH values less than their pI

Breaking strength of pectin gels as a function of pH

Decomposed of pectins Dissolved pectins are decomposed spontaneously by dee

sterification as well as by depolymerization Factors: pH, Aw, Temperature HM-pectins: stable at about pH 3.5- 4, sugars or other agents t

hat lower water activity reduces the rate of degradation LM-pectins: stable at about pH 4-5,

In both acid- and base-catalyzed decomposition, the rate of DEster is faster than the rate of DPoly

Highly esterified pectins are more prone to depolymerization than are LM-pectins or pectic acids

Decomposed of pectins DPoly. At low pH-values is a hydrolysis reaction DPloy. At alkaline conditions is a beta-elimination

reaction Glycosidic bonds to O-4 of an esterified galacturonic a

cid subunit eliminate much more easily than those to O-4 of an nonesteified subunit

The rate of beta-elimination is almost proportional to the amount of remaining methyl ester groups and slow down as they are saponified

Decomposed of pectins Powdered HM-pectins slowly lose their ability to f

orm gels, especially if stored under humid or warm conditions Stored at < 20 C

LM-pectins are more stable, loss should not be significant after 1 year storage at room temperature

Analysis of pectins Degree of esterification (DE)

Washing in 60% 2-propanol (isopropanol)/5% HCl Several washing with 60% 2-propanol (isopropanol) Titrate to the equivalence point with NaOH Saponification

Analysis of pectins Degree of amidation

Heating the sample with excess of NaOH and trapping the evolved ammonia in a known amount of HCL

Acetyl content Alkaline saponification Acidification with dilute sulfuric acid and steam distilla

tion The evolved acetic acid is trapped in a known amount

of NaOH and titrated

Analysis of pectins Average molecular weight

Intrinsic viscosity method Membrane osmometry LC method

2-6 Pectic enzymes Pectin esterases (PEs) EC 3.1.1.11 Polygalacturonases (PGs)

Exo-PGs EC 3.2.1.67 Endo-PGs EC 3.2.1.15

Pectate lyases (PALs) Exo-PALs EC 4.2.2.9 Endo-PALs EC 4.2.2.2

Pectin lyases (PLs) EC 4.2.2.10

Pectin esterases (PEs) Catalyze hydrolysis of methyl ester bonds

Fungal PEs -- optimum pH about 4.5 Bacterial PEs -- pH 6-9

Attack prevailingly next to an unesterified galacturonic acid subunit

Polygalacturonases (PGs) Catalyze hydrolysis of glycosidic bonds

The rate of reaction is inversely related to the DE Optimum pH 4.0-5.5

Exo-PGs Release mono- or di-saccharides from the nonreducing

end Endo-PGs

Attact at random

Pectate lyases (PALs) Catalyze depolymerization via -elimination

Fig 5 273 Only glycosidic bonds to O-4 of an unesterified galactu

ronic acid unit are attacked Optimum pH 8-9.5

Exo-PALs Endo-PALs

Pectin lyases (PLs) Catalyze -elimination at bonds to O-4 esterified g

alacturonic acid units Only endo-PLS are known Optimum pH 5-6 Presence of Ca2+: optimum pH 8

Pectin lyases (PLs) Catalyze -elimination at bonds to O-4 esterified g

alacturonic acid units Only endo-PLS are known Optimum pH 5-6 Presence of Ca2+: optimum pH 8

2-7 Structure and mechanisms of gel formation

To take part in gel formation, a pectin module must aggregate with one or more other pectin molecules

The junction zones must be of limited size because the molecules would otherwise form a precipitate rather than a gel

Citrus, apple and sunflower pectins preparations with acid under hydrolyzing conditions (Powell et al., 1982)

DP is about 25 Because bonds to rhamnose were assumed to be

more labile than ordinary glycosidic bonds in the galacturonan backbone

One rhamnose unit for every 25 galacturonic acid units(regularly distributed)

Apple pectins fractionated by DEAE-cellulose

Rhamnose insertions are very unevenly distributed along the galacturonan backbone (Vries et al., 1982)

Pectin consists of smooth regions and hairy regions rich in neutral sugars predominantly present as side chain

Neutral sugar content tends to be higher if mild conditions have been employed for extraction L-rhamnose, L-arabinose, D-xylose, D-galactose, D-glucose

Pectins from spinach and sugar-beet Ester-linked ferulic acid

has been found in neutral sugar side chains

Formation of a covalent bond between ferulic acid by the action of hydrogen peroxide or peroxidase

Model of a function zone in a high-solids pectin gel

Model of a calcium pectate junction zone

Egg box model of a junction zone in a calcium pectate gel

2-8 Application Pectins are a constituent of all plants and is part

of the natural diet of man Pectins are generally recognized as safe (GRA

S)

2-8-1 Jams and Jellies Pectin has a dominant position as a gelling agen

t in jams and jellies because The natural pectin content in fruits used for jam mak

ing is responsible for the gelation of traditional jam that has been produced for centuries

Pectin is compatible with a natural image of the product

Pectin has good stability at the pH of jams and jellies, even when hot

2-8-1 Jams and Jellies The selection of suitable pectin for a particular application i

s dependent upon the desired texture and the desired gelling temperature

HM-pectins: rapid-set, medium-rapid-set, slow-set The actural gelling rate is dependent on the application conditions

LM-pectins are the possibility if the pH of the product is above approximately 3.5 and/or the soluble solids (SS) concentration is below approximately 55%

Gelling temperature Which gelling temperature is desired is determined

by the filling temp. and the presence or absence of suspended fruit particles in the product Jams should solidify as soon as possible after filling. Fru

it flotation is then stopped before it lead to a too unenen distribution of the fruit particles in the product

Delayed gelation is desirable in the case of jellies so that air bubbles will have time to escape

Filling temperature The desirable filling temperature is in turn restricted

by the size of the jars used Large jars cool more slowly than smaller jars, and

holding at elevated temp. is detrimental to product quality

A relatively low filling temperature is consequently necessary if the product is to be sold in large containers

Which pectin type may be used？ The container size puts an upper limit to the filling

temperature The filling temp. and the desirability or

undesirability of a lag before solidification determine the desired gelling temperature

The desire gelling temp., together with composition of the product, determines which pectin type may be used

Jams, Jellies and Confectionery Jellies Preparations

2-8-2 Acidified Milk Drinks Casein particles of unstabilized acidified milk syste

ms tend to aggregate, especially during heat treatment

A sandy texture may develop and whey formation separation may occur due to sedimentation of the casein

2-8-2 Acidified Milk Drinks A typical use level for pectin in acidic milk drinks is 0.5% The necessary dosage is dependent upon pH, titer, protein co

ncentration, heat treatment and size of casein particles pH 3.5-4.2 Best stability is achieved at relatively high titer value

Typical titers of fruit-flavored acid milk products are 100-120 (mL 0.1N NaOH per 100 mL)

More casein or harsher the heat treatment more pectin is required Large casein particles can not be stabilized efficiently Very small particles require much pectin

Theory of stabilization In unstabilized acidified milk, casein particles that are below

their isoelectric pH are positively charged A repulsion that is not strong enough to prevent aggregation

exists between these particles When pectin is added, it reacts with the casein and neutralize

s the charge, increasing the tendency of particles to aggregate When even more pectin is added to the casein particles, a ne

w repulsion between particles results from a surplus negative charge that is stronger than the original positive charge

2-8-3 Other application Different properties of pectin are utilized in application relate

d to beverages such as orange juice, orangeades, and soft drinks

HM-pectin may be used to increase the viscosity of soft drinks and improve the mouthfeel

It may be used to prevent sedimentation of suspended material in orange juice concentrates with more than 45% SS.

Oil-in-water emulsions in cosmetics may be stabilized with pectin

Numerous patents, most of which related to uses of pectin is in food products

Chapter 3 Cellulose and its derivatives

1. Methylcellulose and its derivatives 2. Hydroxyalkyl and ethyl ethers of cellulose 3. Sodium carboxymethylcellulose

1. Methylcellulose and its derivatives

1-1 Introduction 1-2 Manufacture 1-3 Properties 1-4 Application

1-1 Introduction Etherification of cellulose provides a broad spectrum

of products that includes low-substituted alkyl ethers that are insoluble in water and organic solvents

Alkyl ethers of intermediate substitution that are water soluble

Highly substituted ethers that are soluble in organic solvents but not in water

The methylcellulose and its derivative gums described here are those that are water soluble and classified as hydrophilic industrial gems

1-1 Introduction The term methylcellulose gums is used to refer t

o entire group of products including Methylcellulose (MC) Hydroxypropylmethylcellulose (HPMC) Hydroxyethylmethylcellulose (HEMC)

Methylcellulose gums have broad commercial application in a wide variety of uses and a production of more than 76 x 10 exp 6 kg/year

1-2 Manufacture Cellulose sheet pulp obtained from cotton or wood is c

onverted into alkali cellulose by reaction with sodium hydroxide

Then, pressure reactors are used to etherify the alkali cellulose with methyl chloride and , in some cases, propylene oxide, ethylene oxide, or butylene oxide

Reaction times of 2-10 h Purification takes advantage of the product’s thermal g

elation properties

1-2 Manufacture The crude product is dispersed in hot water, in

which it is insoluble, and is then separated by filtration or centrifugation

Additional washes may be used to improve purity

The wet methylcellulose is dried and milled

Manufacturers of methylcellulose and modified methylcelluloses

1-3 Properties 1-3-1 solid

Methylcellulose gum products are available in powder and granular forms

The primary benefit of powder products is rapid dissolution

Granular products have reduced dusting tendency and are more easily dispersed

Both products may be treatment with dispersing agents to make dissolution easier, but these products can’t be used in foods or in contact with food products

Physical properties of methylcellulose powder and granular products

1-3-2 To prepare solutions Insufficient dispersion may lead to lumping and incomplete

dissolution Application of high-shear mixing devices to help promote

dispersion can cause excessive foaming It is generally recommended that the gum first be mixed

with a formulation ingredient, such as alcohol, glycol, or salt solution. Water is then added to the mixture

The powder can be dispersed in water heated above the gel temperature of the gum

1-3-2 To prepare solutions Solution of methylcellulose gums are pseudoplastic Solution rheology is dependent upon

the molecular weight of the gum its concentration presence of other solutes

Relationship between molecular weight and aqueous solution viscosity

Viscosity as a function of concentration for high-viscosity types of Methocel

Viscosity as a function of concentration for low-viscosity types of Methocel

Gel strength as a function of molecular weight of Methocel products

1-4 Application 1-4-1 Salad Dressing 1-4-2 Dietetic Foods 1-4-3 Fried Foods 1-4-4 Bakery Products 1-4-5 Frozen Dessert

1-4-1 Salad dressing MC and HPMC are used in pourable salad dressings, s

uch as French dressing, to stabilize the emulsion and prevent separation.

Higher molecular weight versions of the gum are preferred for the formulation with the purpose of thicken and stabilize (0.3-1.0% gums)

Higher concentration are used in low-calorie, reduced-oil dressings and in oil-free salad dressings

1-4-2 Dietetic foods Bulking agent in low-calorie foods Partial replacements of digestible carbohydrates with l

ow levels of nondigestible MC gums provides desirable organoleptic properties with reduced calorie content Reduced-calorie salad dressing: 0.3-1.0% gums Dietetic jellies and Preserves :0.5-1.0% gums, palatable Artificially sweetened syrups: 1% MC, smoothness and body Low-calorie beverages: 0.15-0.20% HPMC, mouthfeel and b

ody

1-4-3 Fried foods In batters, dipping solution and sprayed-on coat

ings for meat, fish and French-fried potatoes The gum reduces oil absorption through film format

ion and thermal gelation MC gums hydrophilicity helps to retain moisture du

ring the cooking process, preventing drying out of the food

Batter formulation: 0.5-2.0%

1-4-4 Bakery products Including cake, doughnuts, breads, cookies, fruit pie fillings… Their thermal gelation is valuable in preventing boil-over of p

astry filling and aids in gas retention in cakes during baking Low moisture migration due to their hydrophilic nature impro

ves shelf life and prevents icing dry out Their surfactancy and thickening properties help assure unifor

m consistency by improving emulsification, air entrainment, and ingredient suspension

In frozen baked goods, MC gums retard water migration during freezing and thawing and help inhibit phase separation during freezing

0.07-0.3% base on total ingredients

1-4-5 Frozen dessert MC gums are used in frozen desserts to control

ice crystal size and improve emulsification during processing

0.2-0.5%

1-4-6 others Beer foam stabilizer-- 100ppm or less Barbecue sauce and relish formulations-- 0.3-

1.5% Sausage casings

2.Hydroxyalkyl and ethyl ethers of cellulose

1-1 Introduction 1-2 Manufacture and Properties 1-3 Application

1-1 Introduction The principal, commercial, water-soluble hydroxyalkyl derivati

ves of cellulose are hydroxyethylcellulose (HEC) and hydroxypropylcellulose (HPC)

The derivatives are readily soluble in water and are produced in a wide range of viscosity grades

Their solutions are pseudoplastic, that is, they vary in viscosity depending upon the amount of stress applied

HPC is cold water-soluble and is a true thermoplastic and can be extruded, injection molded or compression molded into flexible film

HEC is insoluble in hot water (> 42 C) and soluble in a broad range of polar organic liquids.

1-2 Manufacture

Water-soluble hydroxyalkylcellulose are manufactured by reacting alkali cellulose with alkylene oxides at elevated temperatures and pressure in a mixture of organic solvents and water

Each unit in the cellulose molecule has three reactive OH groups. Reaction of ethylene oxide or propylene oxide with cellulose also leads to formation of new OH groups

Molar substitution (MS) or degree of substitution (DS)

Viscosity range of aqueous solutions of hydroxyalkyl-celluloses at 25 C and various concentrations

1-2 -1 Preparation of HEC

HEC is produced from alkali cellulose by reacting cotton linters or high-alpha wood cellulose with aqueous sodium hydroxide to produce alkali cellulose (soda cellulose), which is reacted with ethylene oxide in the presence of a water-miscible diluent such as isopropanol or tertiary-butanol

52 parts wood pulp + 450 parts isopropanol + 126 parts 22% aqueous caustic for 1h + 51 parts ethylene oxide heated to 30 C for 1h increase to 35 C maintained for 3h filtered washed with methanol-acetone mixture neutralized with acetic acid dried

1-2 -2 Properties of HEC

Solubility MS > 1.6 : readily soluble in either hot or

cold water Low-viscosity types dissolve more rapidly

than high-viscosity types

Effect of temperature on viscosity -- HEC

The viscosity increases when cooled and decreases when warmed

A convenient nomograph If a solution has a viscosit

y of 60 cP at 25 C The viscosity at 42 C wil

l be ?? cP

Effect of concentration on viscosity -- HEC

Effect of pH on viscosity -- HEC

HEC is a nonionic polymer and therefore undergoes little viscosity change over a pH range of 2 to 12

Solutions show best viscosity stability in the pH range of 6.5 to 8.0

A drop in viscosity results from acid-catalyzed hydrolysis below a pH of 3.0

At very high pH, alkaline oxidation accelerated by heat and light may occur

Rheology of HEC

All solution of HEC are psuedoplastic

Solutions of low-molecular-weight types exhibit less pseudoplasticity

FDA status of HEC

For use in packaging adhesives and resinous and polymeric coatings employed on metal or paper for food packaging

HEC is not cleared as a direct food additives

1-2 -3 Properties of HPC

Solubility Commercial HPCs

have MS > 2.0 Soluble in water bel

ow 38 C, insoluble in water above 45 C

Soluble in many polar organic solvents

Effect of temperature on viscosity -- HPC

Viscosity decreases with increases in temp.

The polymer reversibly precipitates from water at 40-50 C, causing a rapid loss in viscosity

5% NaCl reduced the ppt temp. to 30 C

40% sucrose 20C

Effect of concentration and pH on viscosity -- HPC

Viscosity increases rapidly with concentration

HPC is nonionic and undergoes little viscosity change over the pH range of form 2-12

Thermoplasticity of HPC HPC can be processed by all plastic fabrication

methods The low-molecular-weight types are preferred in

injection and blow molding, where rigidity, hardness, and dimensional stability are important

The medium- or high-molecular-weight types are recommended for most extrusion systems where greater flexibility and higher tensile properties are desired

MW 50,000-1,250,000

FDA status of HPC

Purified HPC is approved as a direct food additive

Toxicity tests indicate that the polymer is physiologically inert

1-3 Application of HPC Organic solubility properties

Thickener in solvent-based adhesives, alcohol-based hair dressings, perfumes, inks,

HPC is widely used as a granulating agent for tablet and capsule mixes in the pharmaceutical industry

HPC films– to coat nuts to prevent oxidative rancidity, coat candies and other confections

Foaming aid and emulsion stabilizer in whipped toppings

3. Sodium carboxymethylcellulose

3-1 Introduction 3-2 Manufacture 3-3 Properties 3-4 Applications

3-1 Introduction of sodium CMC Sodium carboxymethylcellulose (CMC) is a water-solu

ble cellulose ether produced by reacting alkali cellulose with soldium monochloroacetate

CMC was first used as a substitute for starch and natural gums

The purified grade, known as cellulose gum, is used extensively in the food, pharmaceutical, and cosmetic industries

A GRAS product

3-2 Manufacture The traditional process is accomplished in a sigma-blade

mixer The cellulose is steeped in NaOH, pressed, and shredded Sodium monochloroacetate or chloroacetic acid can be mi

xed with the cellulose before or after alkali is added The reaction product is neutralized, dried, and packaged The crude product can be purified by the use of alcohol-w

ater mixtures to extract salts without dissolving the gum

3-3 Properties 3-3-1 Degree of substitution (DS)

Each D-glcopyranosyl unit has three reactive OH group

It is possible to introduce three sodium carboxymethyl groups per unit DS = 3.0

Commercial CMC DS < 1.5 Most common 0.4 < DS < 0.8

Idealized structure of sodium CMC with a DH of 1.0

3-3-2 Uniformity of substitution The first element is the preparation of a uniform

alkali cellulose The proper amount of caustic must be brought into c

ontact with the cellulose fibers in a fashion that ensures uniform distribution

Care in detailed distribution of the monochloro-acetic acid is less critical

NMR is used to determine the relative location of the carboxymethyl groups in CMC

3-3-2 Uniformity of substitution Derivatization of one O

H group on the D-glucopyranosyl unit does not alter the relative reactivity of remaining OH group

The relative rate constant: k2 = 2.14, k3 = 1.00, k6 =

1.58

3-3-2 Uniformity of substitution The unsubstituted regions tend to interact through

hydrogen bonding and generate thixotropy (搖溶性 ) in solutions

Increase in thixotropy with increasing concentration is rough indicator of the relative uniformity of substitution of a given sample of CMC

The longer the average chain length, the more viscous is the solution

3-3-3 Solubility Low-substituted types (DS 0.3 or less) are

insoluble in water but soluble in alkali DS > 0.4 water soluble, DS < 0.4 with high

uniformity of substitution water soluble

Solubility of various sodium CMC-CMC films at various pH values

3-3-4 Rheology of CMC CMC is generally used to thi

cken, suspend, stabilize, gel, or otherwise modify the flow characteristics of aqueous solution or suspensions

Pseudoplasticity: A CMC solution will vary in viscosity as different physical forces are applied to the solution (time-independent shear-thinning)

3-3-4 Rheology of CMC Thixotropy: When long chain polymers associat

e intermolecularly, there tend to develop a three-dimensional structure and exhibit thixotropy (time-dependent shear-thinning)

Solution of medium- and high-viscosity CMC 0.9 < DS < 1.2 pseudoplastic 0.4 < DS < 0.7 with slightly less uniformly substitut

ed thixotropic

Pseudoplastic vs Thixotropic

Thixotropic solutions show hysteresis (遲滯現象 ) loops

The increased shear stress required to break the thixotropic structure reduces the resistance to flow

A pseudoplastic CMC solution instantly reverts to its at-rest viscosity after shear removal

A thixotropic CMC solution requires time for return to its at-rest state

Left thixotropic and right non- thixotropic solution of CMC

3-3-5 Effect of trivalent metal ions Gelation of CMC solution can be controlled to form s

oft, pourable or very firm gels Gradual release of aluminum ions to a CMC solution

results in uniform crosslinking The stiffness of gel depends on the amount of the cro

sslinking Concentration of polymer Metal cation to carboxylate anion ratio pH Polymer chain-length

Aluminum-CMC gels Resistant to nonchelating acids but dissolve slowly in

alkaline solutions High concentration of aluminum salts give more brittl

e gels Low-DS CMC solutions without salt addition also co

uld form the gel More crystalline regions are present in low- than high-DS

CMC Gel formation is probably the result of disaggregation of th

e fringed micelles in the crystalline regions, which provides more potential crosslinking points

3-3-6 Effect of temp. on viscosity Temp. variation has no pe

rmanent effect on viscosity

However, long periods of heating at high temp. tend to depolymerize and degrade CMC

3-3-7 Effect of pH on viscosity CMC solutions exhibit

maximum viscosity and best stability at pH 7-9

pH > 10 some decrease in viscosity

pH < 4.0 less soluble, increase in viscosity

3-3-8 Effect of concentration on viscosity

In concentrated solution There is little tendency for the

counter ions (Na) to move out of the sphere of influence of the charges on the polymer molecules

In dilution solution The cations tend to move away

into the aqueous interpolymer regions, leaving a net charge on the molecules

As dilution continue , the charge density on the chains increase, and the chains continue to uncoil

3-3-8 Effect of concentration on viscosity At higher concentration

Viscosity increases as an exponential function of concentration

A doubling of the concentration causes a tenfold increase in viscosity

Because viscosity is determined in large part by the length of polymer molecules, a wide range of viscosity types of commercial CMC are available MW 40,000-1,000,000

3-3-9 Compatibility CMC is compatible in solution with most water-solubl

e nonionic and anionic polymers and gums, proteins, carbohydrates, salts, and solvents.

Monovalent cations usually form soluble salts Little effect on solution viscosity, clarity

Generally, divalent cations will not form crosslinked gels with CMC Forming hazy solutions with reduced viscosity

Trivalent cations form insoluble salts

Compatibility of CMC with inorganic salt solution

Compatibility with water-soluble polymers

CMC is compatible with most water-soluble gums over a wide range of concentration Low-viscosity types > high-viscosity types

In non-ionic polymer Guar gum , hydroxyethylcellulose, HPC A synergistic effect on viscosity

Synergistic effect on viscosity

Compatibility with solvents

Compatibility with others With carbohydrates

CMC gum thoroughly dissolve in water and sugar is then added increase of viscosity

Dry gum is added to the sugar solution decrease of viscosity

With protein CMC helps to solubilize various proteins and to stabilize t

heir solutions CMC inhibits precipitation of casein in its isoelectric pH r

egion and produces high viscosities

Interaction of sodium CMC (DS 0.7) and soy protein

3-4 Applications Food-grade CMC is widely used because of its

ability to thicken water, act as a moisture binder, dissolve rapidly in both hot and cold aqueous systems

And because it is tasteless, odorless, and forms clear solution without cloudiness or opacity

And because it is physiologically inert and noncaloric

Cellulose gum food applications and properties utilized