Effect of compositional variation in the milling streams on rheological behavior of soft wheat dough and its impact on the end quality of the biscuits. RAHIL AHMED Thesis is submitted to fulfill requirement for the degree of Doctor of Philosophy In Food Science and Technology Department of Food Science and Technology University of Karachi 2018
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Effect of compositional variation in the milling streams
on rheological behavior of soft wheat dough and its
impact on the end quality of the biscuits.
RAHIL AHMED
Thesis is submitted to fulfill
requirement for the degree of
Doctor of Philosophy
In
Food Science and Technology
Department of Food Science and Technology
University of Karachi
2018
II
III
DEDICATION
THESIS IS DEDICATED
TO MY BELOVED
SUPERVISOR
PROF. DR. RASHIDA ALI
&
MY FAMILY
IV
ACKNOWLEDGMENT
First of all, I am very thankful to Almighty Allah who guided me towards the right path of
learning at every stage of my life that helped in performing my duties in the beneficial
way. I take this opportunity to thank the management of English Biscuit Manufacturers
Pvt. Ltd. (EBM) for all the financial support and laboratory facilities to complete the
present work and to apply my knowledge to achieve the targets that is to serve the
company in most beneficial way. My special thanks are due to Dr. Zeelaf Munir and Ms.
Saadia Naveed for their constant encouragement support. I am indebted to my
supervisor Dr. Rashida Ali for her continuous help and motivation. I am also thankful to
my co supervisor Dr. Asad Saeed for his time to time guidance and support. I would also
like to thank the staff at Centre of Excellence, EBM for their technical assistance.
Last but not the least, I wish to deeply express my gratitude to my parents, wife and
other family members for ignoring my duties and negligence towards my commitments
related to home assignments. I am sure that without their constant moral support this
affecting the fermentative activity of baker’s yeast (saccharomyces cerevisiae),
consequently every mill streams will behave differently during baking (Katarina eta al,
2008). The resting and proofing times will be dependent on the type of streams blended
with variable fermentative ability. The values of damage starch, falling number of flour
and amylose content will also influence the fermentative process
1.2.7. Parameters to identify quality of flour streams
There are variety of parameters which indicate the functional properties of streams,
some of these are discussed below. All these values are closely related to mixing, dough
rheology and the baking performance.
a) Ash Contents
Ash content increases with the ER and end streams are usually rich in ash which
are not suitable for biscuit.
b) Polyphenoloxidase PPO
Arabinoxylans present in bran is the major functional component of bran and is
related to the enzyme (PPP) that hydrolyses it, therefore determination of PPO
activity is another valid indicator to evaluate bran contamination in white flour or
for increasing ER (Furest et al, 2006).
c) Protein content
Protein quantity and quality is indirectly a measure of quality of flour. It is
determined by variety of tests such as sedimentation value, LA-SRC, AWRC and
electrophoresis.
d) Particle size
It is the basic requirement in flour mill to evaluate flour quality. Fine particles lead
to produce high damaged starch content with high water absorption.
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e) Falling number (FN)
It measures indirectly α-amylase activity which is related to get strength of starch
gel in dough. High FN means less α-amylase activity and starch molecule will unite
strongly.
f) Moisture content
Normally high moisture in flour supports softness on dough. Excess must be
avoided to present infestation and microbiological attack.
g) Damaged Starch
Low level of damaged starch is required for biscuit manufacturing. Streams which
have damaged starch lower than 25 UCD or less than 6% must be used for biscuit
production, higher value will support bread and pasta making.
1.2.8. Relationship of milling with end quality of biscuits
The end quality of biscuits largely depends on the process of milling and blending. The
choice for selecting break roll streams for further grinding also change the quality of flour.
Approaching towards the tail streams, the composition is fairly stabilized and drastically
changed. The following end quality properties are closely related to the composite flour
that is obtained after blending all the streams.
a. Diameter of the biscuit
The biscuits get reduced in size if major portion of tail streams rich in ash, protein,
damaged starch and bran is included in blending.
b. Height
Height will be decreased if streams of high damaged starch will be used.
c. Weight
Weight will be increased in specific volume i.e. density will be higher if tail streams
are included.
d. Color
The biscuit is related to most of the above values, the higher ash and protein
content will provide biscuit darker in color.
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e. Surface crack/top grain
Tail streams will provide less cracking on the surface due to compact nature of
flour.
f. Mouth feel
Excess PPO activity, ash, protein and damaged starch contents provide hard
texture to biscuit and are responsible for adverse mouth feel.
1.3. Wheat flour
The fine powder after grinding of wheat is called wheat flour.
1.3.1. Composition of flour
1.3.1.1. Proteins
There are four types of protein found in wheat kernel,
a) Albumins (soluble in water)
b) Globulins (soluble in salt solution)
c) Prolamins (soluble in 70 to 85% ethanol)
d) Glutelins (soluble in dilute acid)
On hydration, flour form a viscoelastic mass that is called gluten with activated
network. Gluten is actually composed of two protein, gliadin (Prolamins) and glutenin
(Glutelins).
Glutenins are large polymeric proteins held together by many disulfide bonds. These
proteins give strength and elasticity to dough. Gliadins are smaller monomeric
proteins that are responsible for dough extensibility.
1.3.1.2. Starch
Wheat flour contains generally over 70% starch that is composed of
a) Amylose (25%)
b) Amylopectin (75%)
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Amylose is a primarily straight-chain polymer of α-1,4-linked D-glucopyranose
molecules. Amylopectin is a branched polymer of α-1,4-linked glucose connected by
α-1,6- linked branch points. Starch has the property of absorbing water and cause
swelling when it is heated in excess water.
These properties of starch are important in many aspects relating to flour quality
because they influence the interactions of starch and water in a food system. Starch
granules can be physically damaged during flour milling, increasing their water-
holding ability and susceptibility to be attacked from the enzyme α-amylase.
1.3.1.3. Damaged Starch
The level of damaged starch depends on wheat hardness and milling technique. The
wheat which is harder, needs more force to break out, causing starch granules to be
damaged. Damaged starch increases water absorption of water, make flour
susceptible to α-amylase attack. α-amylase reduces starch into small fragments of
dextrin. Dextrin influences water holding ability and porosity of the dough.
High dextrin quantity softens the dough and make dough sticky, which is unwanted
impact on cookie quality.
1.3.1.4. Pentosans
Pentosans are the constituents of cell walls of wheat endosperm and bran. They are
composed of arabinoxylan which is a polymer with a β-(1-4)-linked D xylopyranose
backbone and branches of L-arabinofuranose.
It absorbs water ten times of its own weight. Pentosans are of both types i.e. water-
insoluble and water-soluble forms, depending on the degree of branching of the
arabinose side chains. A higher degree of arabinose substitution is associated with
higher water solubility.
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1.3.1.5. Lipids
Whole grain wheat contains approximately 2 to 4% and the endosperm about 1 to
2% crude fats.
1.3.1.6. Ash Contents:
The inorganic residue in flour is called ash. It varies in flour and depends on how
milling is efficiently performed. 0.4% to 0.55% ash is usually considered as good
quality flour.
1.3.1.7. Moisture content:
Moisture is already present in wheat and also added during soaking of wheat. Usually
12-14% moisture is found in flour.
1.4. Ingredients other than flour and their functions
1.4.1. Sugar and syrup
Sugar and syrup being part of the recipe influence the various rheological characteristics
of the biscuit dough and the end quality. Excess of sugar reduce extrusion time, density,
consistency, viscosity and development of gluten network (as elastic recovery is
reduced). Spreading and thickness of the biscuit get increased. Reducing sugars like
dextrose, invert syrup, liquid glucose, fructose, high fructose corn syrup (HFCS) are used
as color improvers, HFCS shows better impact. Substitution of small level of glucose,
fructose, maltose, HFCS for sucrose, change the surface cracking pattern of the biscuit.
This shows that reducing sugars are more effective in determining the top grain (surface
cracking) than non-reducing (sucrose). However only glucose or fructose used as sugar
do not affect surface pattern. Sucrose either dissolved or in granular form exhibit surface
cracking because it crystalizes during baking. The appearance and physical properties of
biscuit such as dimensional properties, shape and surface cracking depend on the type
of sugar used because all the sugars vary in their melting point, solubility and
crystallization pattern.
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1.4.2. Milk and role of milk proteins in baking
Whole milk liquid/powder and whey powder/whey protein concentrates (WPC) are
frequently used in biscuit production. Although addition of milk or milk products serves
the basic purpose of flavor and nutritional improvement, however milk components
including proteins play role in altering rheological and textural properties of biscuit.
Caseins show more elasticity and many make the texture harder, WPC has been used in
making gluten-free biscuits (Gaines et al, 2006) and shows its functional property to
participate in making gluten network, whey proteins are very strong non gluten proteins
candidate to replace gluten in gluten free biscuits. Milk ingredients leaving caseins make
dough less elastic and improve biscuit end quality as the softness increases while in
mouth feel it shows better mobility in mouth.
1.4.3. Egg and role of egg proteins
The components of egg are regarded as multifunctional additives in variety of food
system including biscuits, egg is sued to improve texture, volume, color, and flavor apart
from enhancing its nutritional value. Egg proteins play distinct role, like egg white
proteins form stronger, tougher and more elastic gel network than the yolk proteins
which provides color and softness to the biscuit. The protein network gets modified also
during mixing, sheeting and baking
1.4.4. Fat or Shortening
Fat plays many roles in baking, but few critical functions of fat are mentioned
underneath.
Slip melting point which shows the start temperature where fat begins to melt, is one of
the critical and major factor of functions of fat in dough.
a) Dough weakening.
Fat when mixed with flour, surrounds the particle resulting in weakening the gluten
network, resulting in baked products to become softer in texture, easily breakable,
chewable and melt in the mouth.
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b) Creaming
Fat has the tendency to trap air bubbles during beating and mixing of dough which
produces porosity in dough containing many tiny air bubbles that are well trapped in
fat. This is very vital process in baking, the soft and airy texture of the product is
formed due to these air bubbles that expand during baking.
c) Layering
The bakery products other than the biscuit i.e. puff pastry, high melting points fats
are used to produce layers. Fat with high melting points tend to spread inside the
layers of pastry and it will be separated during baking to produce layers or puffs in
products.
d) Flavoring
Commonly all fats that are used in baking must have a plain taste and flavor. This is
required to keep finished product away from changing its own flavor. In rare products
fats are used to impart specific flavor to the baked products for example, using butter
for particular baked goods and lard for meat pie pastry.
e) Emulsion formation
Fat are also used to form emulsion with other ingredients in first stage of mixing
in dough or batter to form dough structure, later flour is added in second stage
of mixing.
1.5. Role of additives in biscuit processing
The additives in baking products have become essential part of the recipe. Additives in
biscuits although were used as flour improvers to ease the processing and to produce the
desired end quality. However, now they serve multiple purposes such as to enhance
nutritive value, to replace the ingredients for cost reduction etc. Variety of substances
are added in bakery products such as oxidizing and reducing agents, enzymes, emulsifies,
hydrocolloids, salts, nutrients etc. The objective of adding each additive is different and
it differ in their chemical nature widely.
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1.5.1. Specific enzymes used in modification of biscuit dough
Enzymes are widely used in improving the functionality of dough. Different proteases
have been added to hydrolyze the gluten proteins (gliadins or glutenins) to make hard
flour soft by reducing the gluten strength of the dough. Amylases are used to adjust
viscosity and flow of the dough while lipases have served the purpose of altering dough
rheology in variety of ways.
Lipases modify the dough by acting as built in emulsifiers because they hydrolyze the fat
present in the dough partially or fully, if fat is partially hydrolyzed then either mono or
diglycerides are produced which are now used as established emulsifiers. Lipases in the
recipe may reduce the quantity of lecithin or may eliminate it completely. Every lipase,
will produce a different emulsifier and so its functions in dough may be desirable or
undesirable.
1.5.2. Emulsifiers in biscuit processing:
Emulsifiers are commonly added as ingredients to improve dough handling and baking
performance. Emulsifiers are responsible for promoting gluten and fat interactions that
makes the end product soft and provide better mouth feel. Lecithin, diacetyl tartaric acid
ester of monoglycerides (DATEM), mono and diglycerides (MGD) are commonly used
individually and in combinations. Biscuit recipe consists fat as a major component next
to flour and role of emulsifiers may hardly be ignored to make a desired product.
Emulsifiers play their role as anti-staling agent in bread. Emulsifiers are responsible for
changing the secondary structure of gluten proteins affecting the texture of end
products.
1.5.3. Oxidizing and reducing agents
Oxidizing and reducing agents are commonly used in flour treatment for variety of
purposes, such as for breaking dough strength/baking performance. Chlorine is used to
bleach the various pigments present in bran. Some oxidizing chemicals act as maturing
agents as chlorine dioxide, acetone peroxide, azodicarobonamide, potassium borate,
potassium iodate (a rapid dough breakdown agent). Potassium iodate and
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azocarbonamide are fast acting oxidant and give similar effect as given by activated
dough bond compound. The reducing agents break the disulfide bridge of the large
glutenin molecules and make protein molecule size smaller than get hydrated easily and
dough mixes well reducing the mixing time. The reducing agents such as cysteine, sodium
bi-sulphite and sodium meta bisulfite are often used as flour improvers.
1.5.4. Hydrocolloids
The significance of functional importance of hydrocolloid in modifying dough rheology
and baking performance is being gradually understood in baking industry. Hydrocolloids
are hydrophilic biopolymers widely distributed in food systems, they affect water take up
by different molecules in the recipe by interacting with water ions and thus alter the
swelling, gelatinization, viscosity and gelling properties of the mix (dough). Hydrocolloids
are used as improver in bread, cake, biscuit and other bakery products. Some of the
hydrocolloids have been used as gluten replacers in the gluten free products as they are
capable of inducing viscoelastic, hydration and gas binding (gas retaining) properties.
Common hydrocolloids include gums (xanthan, guar, arabic), carbomethoxy cellulose
(CMC), non-starch polysaccharides (NSP) such as celluloses and hemicelluloses, beta
glucan, arabinoxylans, dietary fibers etc. Some of the emulsifiers also act as hydrocolloids
because they promote lipid gluten and lipid starch interactions in dough making process.
The gel rheology of the dough gets improved in presence of hydrocolloids which seems
to be a requisite for establishment of continuous network structure of the dough.
1.6. Mixing
1.6.1. A process of dough development
Mixing is an integral and the most critical part of any baking industry because the
mistakes you make here will appear in baking i.e. in end quality and there will be no
possibility for correction. Mixing is the process where all the ingredients in appropriate
amounts are blended and they interact to achieve the uniform distribution of each to
produce a mass of desired consistency, the mass is named as “dough”. So mixing is a
process of dough development that is highly important, complex, focal and need skilled
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handling. Mixing time of the dough depends on the recipe of biscuit and may take 5-25
minutes.
1.6.2. Reactions in mixing
Variety of reactions take place during mixing to properly develop the dough. These
reactions may be inter ingredients or intra ingredients for example a component of flour
say protein may interact within itself or may react with another component (starch). It is
also possible that protein/starch in flour may react with sugar, fat or other ingredients.
The dough development is therefore a process of multiple visible and invisible stages,
where variety of reactions are taking place to develop gluten network, gluten-starch
matrix formation etc. The other molecules (ingredients) are embedded in the network
uniformly to produce desired viscoelastic mass or the dough. Some of the visible stages
of dough development are briefly discussed here, which are actually the outcome of
chemical reactions (invisible)
a. Formation of many electrostatic bonds between water molecule and
protein/starch.
b. Formation of new di-sulphide bridges that generate gluten network.
c. Protein starch linkages that develops protein matrix
d. Starch- starch interactions that shape a starch granule embedded in
protein network.
e. Non peptide linkages formation as a result of reactions of protein with
oxidizing and reducing agents
f. Enzymatic hydrolysis of peptide ester linkage of fats, acyle bond of
starches and their interactions in between themselves.
g. Formation of starch – fatty acids enclosures.
In fact many more such reactions are simultaneously occurring that finally give the shape
to dough. Some stages in mixing which are very visible, are being briefly discussed here.
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I. Pick up
It is the process of hydration of each ingredient but the water taken up is not
absorbed or interacted. The mix is sticky with lumps and is cold. It shows ratio of
the hydrophilic and hydrophobic ingredients in a recipe.
II. Initial development
Water is penetrating and acting as a bridge between molecules, dough is smooth,
dried and hold temperature gets warmer.
III. Clean up
Dough is getting as one mass and scattered ingredients interact firmly to make it
stiff and together. Changes in color are obvious because of molecular interaction.
The dough now is lumpy, irregular and hard. It is the “under developed dough”.
IV. Final development
During the process of further mixing the dough has gained elasticity, desired
gluten network is at final stage i.e. s-s-bridges with in the glutenin and in gliaden
– glutenin have been sufficiently formed, arabinoxylan and starch interlinkages
have been developed to hold other molecules to provide the appropriate
viscosity. The temperature of the dough is suitable for handling, the dough which
at this stage may be called as the “optimal dough”, the dough ready to be baked.
V. Let down
The dough is very warm and viscous with more flow and less elasticity. The
molecular interactions if exceed than desired, the dough becomes very soft and
mobile.
VI. Breakdown
The inter molecular bridges i.e. s-s-and ferulic acid, protein-protein cross linking,
starch-protein, starch – starch (amylose-amylopecin with fat linkages) are
breaking and dough is getting weak, beginning to liquefy. The dough at this stage
may be called as “over developed”.
VII. Ideal dough
The ideal desired dough / optimal dough for each product (for each recipe) is
different and is obtained by controlling of the temperature at each stage, mixing
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time and speed of mixer etc. Its temperature, density, weight, viscosity etc.
should be recorded as a check parameters to control quality of the dough that
determines quality.
1.6.3. Identification of optimal dough:
Optimal dough is the dough which produce the desired product on baking. It must be
thoroughly examined before baking because once the end product is obtained, the
process is irreversible. The parameters (tests) to assess the quality of optimal dough must
be highly reliable and dependable. Some of the tests to identify optimal dough are
discussed below.
a. Baking performance
The most reliable is the baking test, however it takes time. Some rheological tests using
Mixolab, texture analyzers and alveograph etc. provide information about pre baking
quality of dough. However quick tests are needed to decide whether the dough should
be baked or recycled such tests are discussed here.
b. Dough density
It predicts dough baking performance and end quality. The shape, weight and
dimensional characteristics are evaluated by studying the density of dough which may
easily be determined by dipping (immersing) a known weight of dough into an immiscible
liquid (water), the formula weight/volume will give the density.
c. Temperature of dough
The temperature of the dough before entering the oven is very important and should
coordinate with the temperature of 1st oven zone. Dough temperature at the beginning,
middle stage and end stage is also important. The dough temperature rises because of
inclusion of heat of hydration, heat of friction and environmental temperature that affect
the intermolecular reactions and the end properties. The rise in temperature during
mixing may be approximately calculated by friction factor which is defined as the value
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used to compensate for the increased length of time. The friction factor is calculated by
the following formula,
3 x t 0C (dough) - t0C(room)+t0C (flour) + t0C(water) = Friction factor
d. Water absorption
Known amount of dough placed on a paper and pressed with a known weight will
produce wetted area on paper that is inversely proportional to water withheld and is
related to texture, surface crack etc.
e. Fat absorption
It is determined in the same way as the water absorption and is related to color and the
softness of the biscuit.
f. Hexane stability test
It gives amount of unabsorbed fat in the dough which is related to color, spread ability
etc. Expert bakers use their own way of thumb pressing, area of fat on filter paper, stretch
ability etc. Such tests at the end of mixing and before baking are important to reduce the
unwanted wastage.
g. Thumb Impression
Smooth dough when pressed with thumb makes depression, how quickly the dough
detains its original appearance predicts the dough baking performance.
Expert bakers may feel the dough behavior well in baking and such simple tests may
further help to predict the end quality and in identifying the desired dough.
1.6.4. Dough as a predictor of end quality
Bakers have to realize that dough before baking is the true predictor of end quality and
during dough development, variety of changes in process may change the dough
rheology and baking performance. As multiple reactions are going on during dough
development, it is necessary to promote certain reactions and to restrict also
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considerable reaction to achieve the best performance of the dough. “Resting of the
dough” for a short period of time may be a good option that may reduce mixing time and
to save energy. Many of the reactions presently going on may get time to be completed.
Resting of dough is often desirable if enzyme are used.
1.7. Baking
1.7.1. Reactions in baking
It is interesting to see that how a flattened piece of dough get the attractive shape
appealing and a yummy taste just after spending few minutes in various sections of oven.
It is because the complex molecules as protein, fat, starch interact in multiple ways in
presence of water and heat. We have already hydrated these molecules during mixing
and provided the facility to them to swell that initiate inter molecular associations that
promote reactions in baking. Baking is actually a process of series of chemical reactions
responsible for visible physical changes i.e. formation of biscuit shape, appearance and
flavor. Some of these reactions are briefly discussed here.
a) Vaporization and mobility of water
The water present in dough vaporizes slowly as the dough enters in the oven. The
vapors moves horizontally (from center to sides) and vertically (from bottom to top)
that causes dough to expand and it dries gradually forming the structure. The
hardness, color, height and diameter of the biscuit may be controlled by varying the
speed of oven band, temperature and humidity in each zone of oven that determines
the texture of the biscuits percentage of moisture loss in each zone is a control of
quality of biscuit.
b) Caramelization
The process of caramelization brings three distinct changes in biscuit, firstly color,
secondly flavor and thirdly texture (crispiness). Caramelization in brief is a process of
burning of sugar in absence of moisture that causes color change from yellow to
brown, flavor development as burnt, bitter, acrid texture and formation. The above
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observation are a result of multiple, chemical reactions between unsaturated
compounds forming complex polymers that are mostly saturated.
c) Maillard reaction
Maillard reaction is a group of reactions that includes condensation, addition and
polymerization reaction in series. It begins when water evaporates from dough and
condenses in dough an group of a protein to react with aldehdic group of starch to
form an amide. Many such reaction products go through polymerization to produce
compounds of brown color, burnt flavor and hard texture. Millard reaction also plays
key role in giving appearance, color and taste to biscuits.
d) Protein modification
Variety of proteins are present in dough which change or modify their structures when
heat is provided and water evaporates. Firstly coiled structure of protein is decoiled
and it aggregates that change in protein is known as denaturation or coagulation of
protein. This thermal denaturation at a temperature of 60-70 °C causes protein to
release water during uncoiling the released water (Proteins absorbs 31% water) is
taken up by starch which at further higher temperature > 74 °C gets gelatinized around
air bubbles, forming rigid structure due to protein and starch binding. All these
reactions help in texture formation of biscuit. Texture development is a complex
process of multiple reaction where ingredients added water and thermal environment
play their roles.
e) Starch gelatinization
Starch gelatinization is at least a three step process, firstly the starch granules hydrate
themselves, secondly the starch starts swelling at 40 °C, thirdly they start losing water
at higher temperature (simultaneously they bind protein) to from gel and finally to
become rigid in structure by losing water from gel. Starch is the most abundant
molecule in dough as flour consists nearly 68-82% of starch. Texture formation is
therefore mostly controlled by starch gelatinization.
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f) Enzyme inactivation
The two groups of enzymes that mostly participate in baking are amylases and
proteases. Amylases accelerate the starch break down that makes dough more fluid,
mobile and promotes expansion. If enzyme is activated early the expansion or
spreading will be limited. Similarly proteases cause protein to hydrolyze that release
water also and will affect starch gelatinization and starch binding. Protease will cause
structured change.
g) Cell structure formation
The air bubbles in dough get reduced in baking depending on the heat provided. The
cell structure is different in crust (upper surface) and crumb (inter structure) the size
of cells in both are different and they are more compactly packed in crust as compared
to crumb, that has to be controlled in baking to give the desired mouth feel, chewing
and biting properties. All these reactions control the end quality.
1.7.2. Role of Ovens in Baking
Industrial baking ovens are generally called as tunnel ovens they consist of long
conveyors which carry the biscuit pieces through a heated tunnel section of the baking
chamber. The length of oven may differ from 25 meter to 100 meter. Two type of the
conveyor bands are available referred as wire-mesh and carbon steel band. The time of
baking and temperature are the two major factors in controlling the baking performances
of biscuit. The baking time is set if conveyor is driven with variable speeds.
1.7.3. Baking Zones
Industrial baking ovens are usually divided into zones accordingly to the differences in
the temperature and humidity which are controlled in zones along the length of the oven.
Most of the industrial baking ovens are based on 4 to 6 zones. The purpose of the
different zones system is to adjust temperature and humidity at suitable values during
the baking. The environments of the zones thus created will boost the developing of the
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biscuit structure at suitable parameters such as moisture, top grain and color to get the
desired end quality.
The moisture removed from the biscuit dough depends on the extraction unit in every
zone which is linked to the speed of the conveyors. A fan is used to draw moist air from
baking tunnel for the exit of the moist air to chimneys and finally to atmosphere that
determines the extraction units.
There are three types of oven used in professional baking oven,
I. Radiant - Direct gas fired ovens and indirect radiant that is called cyclotherm
ovens
II. Conduction– The mesh bands or steel bands that are used pre-heated
III. Convection – They may be direct and indirect.
1.7.4. Hybrid ovens
Commercially a combination of different oven types are used in the form of zones that is
called “hybrid” or “combination” oven. The advantage of hybrid ovens is that different
heat transfer modes may be used at different stages of the baking process.
Table 2: Combination of zone used for commercially baked biscuits in Hybrid ovens
Zones
For semi hard/Sheeted product
i.e. biscuit and cracker
(wire mesh band)
For soft product i.e. cookie
(steel band)
01 Direct fire Cyclotherm
02 Direct Fire Cyclotherm
03 Cyclotherm Cyclotherm
04 Convection Convection
05 Convection Convection
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2. CHAPTER: MATERIAL AND METHOD
2.1. Materials
Materials are separately discussed in each study or investigation. Please refer sections
“3.1.2.”, “3.2.2.”, “4.1.2.”, “5.1.2.”, “5.2.2.”, “5.3.2.”, “6.1.2.” and “6.2.2.” for the
description of materials.
2.2. Methods
2.2.1. Physicochemical Analysis
Instrumental Analysis
2.2.1.1. Moisture Content
Brabender Moisture Tester (Germany) was used to determine moisture contents of flour.
9 - 11 gm flour was dried at 155 °C as per AACC approved method no. 44-19.
Note: Results of moisture analysis have been discussed in the sections i.e. “3.1.3.1.”,
“3.2.3.1.”, “4.1.3.3.”, “5.1.3.1.”, “5.3.3.1.”, “6.1.3.1.” and “6.2.3.1.”
2.2.1.2. Analysis using Kernelyzer
Total protein, zeleny value and ash contents were analyzed by using Brabender
Kernalyzer. Ash is a critical parameter which identifies the flour quality with respect to
milling efficiency. Amount of ash in flour is also a legal requirement of PSQCA (Pakistan
Standard Quality Control Authority) which need to be fulfilled according to a baking
industry.
Normally ash is determined through muffle furnace method which takes at least 6 hours
to produce the result, it also involves manual handing which produce results where
accuracy may be challenged. Kernelyzer is a nondestructive testing machine which gives
results in seconds. Keeping time limitation and accuracy in result, Kernelyzer is used in
most of the commercial industries.
Note: Results Kernelyzer have been discussed in the sections i.e. “3.1.3.1.”, “3.2.3.1.”,
“4.1.3.2.”, “4.1.3.3.”, “5.1.3.3.”, “5.2.3.1.”, “5.3.3.1.”, “6.1.3.1.” and “6.2.3.1.”
29
2.2.1.3. Vibratory Sieve shaker to determination the particle size
The distribution of particle size in flour was measured by a vibratory sieve shaker
(Oberstein, Germany). Two sieves of 160 to 125 micron was used with vibration of 2 mm
amplitude for the time period of 10 min.
Note: Results of particle size analysis have been discussed in the sections i.e. “3.1.3.1.”,
“3.2.3.1.”, “4.1.3.3.”, “5.1.3.3.”, “5.2.3.1.”, “5.3.3.1.”, “6.1.3.1.” and “6.2.3.1.”
2.2.2. Farinograph Analysis
The flour behavior during dough making (rheological properties) were analyzed on
Brabender Farinograph (Duisburg, Germany) as per approved method of AACC (method
54-21). Farinograph Quality Number (FQN), Water Absorption (WA), Dough Stability Time
(DST), Dough Development Time (DDT) and two type of Degree of Softening (DoS) (ICC -
12 min after peak time and 10 min after beginning of curve) were determined.
The flour samples (300 gm) consisting 14 % moisture content were placed separately in
the mixing bowl of Farinograph. The line of 500 Farinograph Unit (FU) was reached, water
was poured by using already installed burette.
a) Dough development time (DDT)
DDT that is also called “peak” or “peak time” is the time when water is first added till it
reaches to maximum consistency of dough and dough moves slowly. It also indicate the
mixing time of dough.
b) Dough stability (DST)
Dough stability time is the time of difference in arrival and departure time. Arrival time
shows the time when peak first touches 500 FU line while departure is the time when
peak departs from 500 FU. DST is a measure of dough strength that how long the dough
may remain unchanged and is not deformed.
30
c) Degree of Softening (DoS)
DoS of the dough is measured in two ways. It is the difference in torque (FU) from peak
at the top of the curve measured either 12 min after peak time or 10 min after the
beginning.
d) Water Absorption (WA)
It is the amount of water required to be absorbed by the flour to form a consistent dough
at 500 FU. The water absorption value changes according to the quality of flour and the
ingredients in recipe. Hard flour need more water to reach required consistency of the
dough.
e) Farinograph Quality Number (FQN)
Farinograph quality number suggests the overall nature of the dough. High FQN reflects
strong dough network, while low FQN indicates weak dough.
Note: Results of farinograph have been discussed in the sections i.e. “3.1.3.2.”,
“3.2.3.3.”, “4.1.3.4.”, “5.1.3.2.”, “5.2.3.3.”, “5.3.3.2.”, “6.1.3.3.” and “6.2.3.2.”
2.2.3. Micro Visco-Amylo-Graph (MVAG) Analysis
MVAG (Brabender, Duisburg, Germany) was used to determine pasting properties of
starch present in wheat flour. Approved method of AACC (AACC Method 22-12) was used
to analyze wheat flour. A 15 gm flour sample was weighed and transferred into the bowl
provided with MVAG and then distilled water around 100 ml was added. The quantity of
water was adjusted as per the moisture content present in flour. Slurry was initially
formed by shaking with hands, then the bowl was fixed in MVAG. Slurry was stirred at
160 rpm and heated to 35°C for 10 sec and then heated to 95 °C for 7.3 min. During the
holding period, slurry was held heated at 95 °C for 15.7 min. Finally it was cooled to 50
°C for a period of 7.7 min. Beginning of Gelatinization, Max Viscosity/Peak Viscosity (PV),
Break-Down (BD) and Setback (SB) were estimated.
31
a) Pasting Temperature
The capacity of starch to swell depends on ratio of amylose and amylopectin, their chain
length, total concentration and chemical structure of the two component of starch
granule. The swelling shows the ability of starch molecules to inbide water and depends
on the pasting temperature which is defined as the temperature at which the fluid gets
viscous. It also determines beginning of gelatinization. The MVAG measures the pasting
temperature that helps to regulate the temperature of zone of baking oven. The excess
of starch granules lowers the pasting temperature while small molecules as
glucose/maltose lead to high pasting temperature.
b) Peak Viscosity/Maximum Viscosity
Peak viscosity of the starch molecule is related to its ability to swell and form paste on
heating in water, if the paste is concentrated viscosity will be higher because the pins of
the mixer will resist during stirring and will show higher viscosity. The ability of the paste
to resist movement during stirring is called the peak viscosity. It is related to overall end
quality of biscuit.
c) Hot Paste Viscosity
It is the viscosity measured at the end of heating process and determines the mobility of
swollen starch granules after cooking for 20 minutes. Viscosity at this stage is decreased
and is known as the breakdown viscosity. Which is calculated by subtracting the hot paste
viscosity from peak viscosity. The hot paste viscosity is related to hardness of the end
product.
d) Cold Paste Viscosity
It is the viscosity measured at the 300C or the 500C and is higher than the hot paste
viscosity or breakdown viscosity because the amylose molecules now reunite making
the paste thicker. This phase is refereed as retrogradation of starch when more H-
bonds are formed between adjacent hydroxyl groups of amylose units. The cold paste
viscosity is related to mouth feel property of biscuits.
32
e) Setback Viscosity
The SB viscosity involves recrystallization of starch which shows the closing of double
helices and viscosity increases. It is calculated by subtracting peak viscosity from cold
paste viscosity which is also named as final viscosity. All the viscosities at cold
temperature are related to chewing, biting or mouthfeel properties and elaborate the
eating quality of the biscuit or the biscuit texture.
Note: Results of MVAG have been discussed in the sections i.e. “3.1.3.3.”, “3.2.3.4.”,
“5.2.3.4.”, “5.3.3.3.”, “6.2.3.3.” and “6.1.3.4.”
2.2.4. Glutomatic Analysis
Different analysis on gluten proteins were conducted on Glutomatic System - 2000
(Perten, Sweden) as per approved method 38 - 12 (AACC, 2000). The dry gluten (DG), wet
gluten (WG), passed gluten (PG), retained gluten (RG), gluten index (GI) and water
binding capacity (WBC) were the parameters analyzed using Glutomatic System. 10 gm
flour sample was placed on cups with polyester sieve and fixed in the washing chamber
of Glutomatic. 2% saline water was used to wash the flour for 5 min. The residue i.e. wet
gluten was collected on cups and then placed in centrifuge machine to get passed and
retained gluten separated through a perforated mesh already installed inside the holder
cup.
a) Gluten Index:
The Gluten Index is a measure of gluten strength or the gluten network of the dough
and is calculated by the formula GI = (Retained gluten)/100.
b) Wet Gluten:
Wet Gluten is a predictor of few qualities of the flour. It measures water binding
capacity of the gluten proteins, thereby indicating the behavior of gluten proteins
during mixing and baking. The amount of wet gluten shows hardness of the flour and is
measured by Glutomatic 2200 using method 38-12 (AACC-2000) proteins.
33
Note: Results of glutomatic proteins have been discussed in the sections i.e. “3.1.3.1.”,
“3.2.3.5.”, “4.1.3.3.”, “5.1.3.4.”, “5.2.3.5.”, “5.3.3.4.”, “6.1.3.5.” and “6.2.3.1.”
2.2.5. Determination of Damaged Starch Content by SDmatic
Damaged Starch content was analyzed by using Chopin Sdmatic. The Sdmatic from
Chopin is designed to measure starch damage rate of the flour in Ai %( iodine absorption)
and in UCD (Chopin Dubois Unit). The Sdmatic works on the Medcalf and Giles Principle
(1965) to measure the starch damage rate of flour.
Briefly describing, 120 ml of distilled water in plastic bottle is taken, 1.5 grams of citric
acid, 3 gm of potassium iodide with 1-2 drop of sodium thiosulphate at 0.1 mol/l were
added. Bottle was shaken for seconds and then poured into a reaction solution in reaction
bowl of Sdmatic system. Reaction bowled was placed in the Sdmatic and folded down the
arm. 1 gm of flour was weighed in the spoon and placed in the Sdmatic. Flour weight,
moisture and protein level were fed in the software and the test was started. Results
were shown in UCD, % according to AACC 76-31and also in Farrand.
Note: Results of DS have been discussed in the sections i.e. “4.1.3.3.”, “3.2.3.1.”, “5.1.3.3.”
and “5.2.3.1.”
2.2.6. Scanning Electron Microscopy (SEM)
SEM (Analysis system, Model JEOL-2300) was used to evaluate dough microstructure
according to Prabhashankar and coworker (2004). Samples of dough were kept in hexane
for 16 hr to defat it. After fat removal, dough was dried by freezing for 5-6 hr. For sample
preparation to analyze in SEM, dried dough was cut (transversally) into fine slices by using
blade considering no damage of the dough structure. After mounting on the holder
further studies were taken place to produce picture.
Note: Results have been discussed in the section of “6.2.3.4”.
34
Chemical Analysis
2.2.7. Solvent retention capacity
Different type of Solvent retention capacity (SRC) analysis were conducted as per the
approved method of AACC 56 - 11 (AACC 2000). All SRC are discussed below,
a) Water SRC
1 gm of flour sample (each) was added in tube with 5 ml of water. The suspended flour
samples were held hydrated for the period of 20 min (shake for 5 second after 5, 10, 15,
and 20 min). After 20 min tube were placed in centrifuge tube with 1,000 rpm for the
period of 15 min. The supernatant in the tube was decanted and then tube was placed
on a paper towel at 90° angle to drain it for 10 min. The remaining centrifuged part of
flour was weighed. The SRC value was calculated as per the method derived by Haynes
and coworkers (2009). The analysis for each sample was conducted in duplicate.
b) Sucrose SRC
1 gm of flour sample (each) was added in tube with 5 ml of 50% sucrose. The suspended
flour samples were held hydrated for the period of 20 min (shake for 5 second after 5,
10, 15, and 20 min). After 20 min tube were placed in centrifuge tube with 1,000 rpm for
the period of 15 min. The supernatant in the tube was decanted and then tube was
placed on a paper towel at 90° angle to drain it for 10 min. The remaining centrifuged
part of flour was weighed. The SRC value was calculated as per the method derived by
Haynes and coworkers (2009). The analysis for each sample was conducted in duplicate.
c) Lactic Acid SRC
1 gm of flour sample (each) was added in tube with 5 ml of 5% lactic acid. The suspended
flour samples were held hydrated for the period of 20 min (shake for 5 second after 5,
10, 15, and 20 min). After 20 min tube were placed in centrifuge tube with 1,000 rpm for
the period of 15 min. The supernatant in the tube was decanted and then tube was
placed on a paper towel at 90° angle to drain it for 10 min. The remaining centrifuged
35
part of flour was weighed. The SRC value was calculated as per the method derived by
Haynes and coworkers (2009). The analysis for each sample was conducted in duplicate.
d) Sodium carbonate SRC
1 gm of flour sample (each) was added in tube with 5 ml of 5% sodium carbonate solution.
The suspended flour samples were held hydrated for the period of 20 min (shake for 5
second after 5, 10, 15, and 20 min). After 20 min tube were placed in centrifuge tube with
1,000 rpm for the period of 15 min. The supernatant in the tube was decanted and then
tube was placed on a paper towel at 90° angle to drain it for 10 min. The remaining
centrifuged part of flour was weighed. The SRC value was calculated as per the method
derived by Haynes and coworkers (2009). The analysis for each sample was conducted in
duplicate.
Note: Results have been discussed in the sections i.e. “3.1.3.4.”, “3.2.3.2.” and with other
physicochemical analysis.
2.2.8. AWRC profiles of flours:
The AWRC was conducted as per approved method of AACC 56-10, 1 gm of flour sample
(each) was added in tube with 5 ml of NaHCO3 solution (8.4g in 1 liter). The suspended
flour samples were held hydrated for the period of 20 min (shake for 5 second after 5,
10, 15, and 20 min). After resting for 20 min, the tubes were centrifuged at 1,000 rpm for
the period of 15 min. The supernatant in the tube was decanted and then each tube was
placed on a paper towel at 90° angle to drain the fluid for 10 min. The remaining
centrifuged part of flour was weighed. The AWRC value was calculated as per the method
derived by Haynes and coworkers (2009). The analysis for each sample was conducted in
duplicate.
Note: Results have been discussed in the section of “5.2.3.2.”
2.2.9. Statistical Analysis
The simple statistical techniques using Microsoft Excel (2010) were mostly used to
analyze the data. Tools including linear correlation coefficients between different
36
parameters, scattered chart and line/bar chart were utilized. The SPSS statistical software
(version 20) was used for SEM study.
The values shown in each investigation are a mean of at least three readings.
The reason of including very simple statistical analysis in the study is to focus the milling
industries in Pakistan who are not well developed, they can easily interpret and apply
results in their industries to get the benefit from these studies.
2.2.10. Evaluation of biscuit end quality
The end quality of biscuits was evaluated under the following heading
a) Dimensional analysis
The biscuit dimensions i.e. size, thickness including weight were measured and recorded
as per AACC method (10-31B). Sample for measurement was randomly selected. The
diameter of the biscuit was measured in mm by turning at different angles three times
and the mean value is reported. The thickness of biscuits were measure by placing eight
biscuits in a column and taking average of one biscuit in mm.
The cookie factor/spread ratio was calculated by dividing width (W) by height (H)
according to Colombo et al (2008).
b) Textural analysis
The hardness of biscuit was measured by UTM (Zwick/Roel). Force was calculated on N.
c) Sensory analysis
The 10 trained panelists from English Biscuit Manufacturers Pvt. Ltd. Conducted the
sensory evaluation by using a nine point Hedonic scale. One (1) represented “extremely
dislike” and nine (9) represented “extremely like”. Texture, color, flavor, taste and overall
acceptability level were the attributes for sensory evaluation.
Note: Results have been discussed in the sections i.e. “3.2.3.6.”, “5.3.3.5.”, “6.1.3.6.”,
“6.2.3.5.” and “6.2.3.6.”
37
3. CHAPTER: WHEAT MILLING AND ITS INDUSTRIAL APPLICATION
3.1. Study of milling streams used in the production of commercial flours
to be utilized in biscuit making industry.
3.1.1. Foreword of the study
Miller, usually face difficulties to produce flour as per customer requirement due to the
uncontrolled supply chain of wheat in Pakistan especially if they have to supply same
quality of flour for longer period of time or permanently. Milling industries are also in
transition period to be modernized by installing state of the art plants and inducting
excellent human resource to face the challenge of supplying flour as per customer need
inspite of the issue of unavailability of required type of wheat kernels.
The study was conducted to evaluate the physiochemical and rheological properties of
milling streams produced in a mill to identify required quality of flour and match with the
different specifications for the customers by mixing selected streams to get composite
flour.
38
Figure 3: Flow chart of milling streams for flour collection
PN: Numeric values are representing the sieve size in micron, alpha numeric values are
representing the streams name. Purifier is actually called Suji machine in Pakistan.
39
3.1.2. Material and Method:
Please refer to chapter 2 for detail description of the methods, however only specific
material and method related to the topic are discussed here.
3.1.2.1. Material
Soft wheat from Punjab origin was milled commercially in Garibsons Pvt. Ltd. Port Qasim,
Karachi, Pakistan. Total 35 flour streams (all type) were studied and samples were
collected accordingly.
3.1.2.2. Information on milling streams used in the study
The final product or the composite flour as commercially practiced in Pakistan is
produced by mixing of the various milling streams/passages as mentioned below
(definition and description were discussed in table 3).
a) Break Streams
b) Middling Streams
c) Fine and Coarse Semolina Streams
d) Semolina Overtail Streams
The final product actually represents the composite flour or a mixture of all the above
mentioned streams. The 132 micron sieve size of sifter was fixed at the mill for getting
flour to be mixed in last stage for adjusting the quality and quantity of the final product.
Some flour streams after sieving from 150 or 180 micron sieves were also used to
increase the extraction rate of flour and to meet the customer order (required quantity).
However, all other quality parameters were achieved within the range of customer’s
specification even after mixing the larger particles size flour.
Table 3: Streams names, types and description
S. No Strea
ms Name
Name of Streams after combining similar streams
Type of Streams
Description of streams
1 B1A
1st Break Break Streams
Wheat is broken by the set of grooved rollers and converted into the many fractions varying in particle size. All fractions are passed through
2 B1B
3 B1C
4 B2A 2nd Break
40
5 B2B the different sieves in huge sifters. The particles which are collected after the end of sieve of 132 or 180 micron are diverted to be mixed into the end product. Whereas the rest of the fractions are further processed by smooth rollers (reduction rollers) to extract remaining flour of different particle size.
6 B2C
7 B3A
3rd Break 8 B3B
9 B3C
10 B4A
4th Break 11 B4B
12 B4C
13 B4D
14 B5A 5th Break
15 C1A Coarse - C1A
Fine and Coarse
Semolina Streams
Portion of ground wheat from break rolls, which has particle size in between 1020-820 micron to 720-530 micron goes to purifiers for the separation of bran, then these fractions are processed by set of rolls and streams are produced called coarse semolina streams, whereas particle between 720-530 to 280-270 micron goes to other purifiers, including the other set of RR and these passages called fine semolina streams. The flour of particle size that is collected after the end of sieve of 132 or 180 micron are diverted to be mixed into the end product flour. Rejection of both the purifiers are diverted to C1B whereas end residue is diverted to bran rich products.
16 C2C Fine - C2C
17 C2A Fine - C2A/B
18 C2B
19 C3A Fine - C3A
20 C1B C1B Semolina Overtail
Streams/ Rejection
from Semolina Streams
Rejection/retained of purifier (Suji machine), goes to other roll sets for further grinding. Flour received after sieving from 132 micron sieves are diverted to be mixed in the final product.
21 C4A C4
22 C4B
23 C5A C5
24 C5B
25 C6A C6
26 C6B
27 D1A D1
Middling Streams
Retained wheat part on 132 or 180 micron sieves from the break roller, goes to other set of smooth rollers for further grinding. In each roller set, flour is achieved after passing it through 132 micron sieve.
28 D1B
29 DD1A DD1
30 DD1B
31 R1A R1A
32 C7A C7A
33 C7B C7B
34 C8A C8
35 C8B
41
The large scale size flour mills usually use more than one set of two rolls for same streams
to get the high grinding rate (extraction rate).
The flours from roller sets consisting similar values were mixed and the number of milling
streams were reduced to 19. Underneath discussion is based on the 19 milling streams.
Table 4: Milling streams type and details
S. NO Streams/Passages # of
streams Name of streams
1 Break Rolls 5 1st, 2nd , 3rd, 4th and 5th Break
2 Fine and coarse
semolina
4 Coarse C1A, Fine C2C, Fine C2A/C2B
and Fine C3A
3 Semolina Overtail 4 C1B, C4, C5 AND C6
4 Middling 6 D1, DD1, R1A, C7A, C7B AND C8
The numbers of streams mentioned above were assigned by the Mill as themselves that
differ from mill to mill.
3.1.3. Result and Discussion
3.1.3.1. Physicochemical Analysis of Milling Streams
3.1.3.1.1. Moisture
The moisture is a critical parameter for optimizing flour quality for the manufacturing of
biscuits and cookies. It plays vital role in indicating the flour behavior in dough
development and water may need adjustment in the recipe. The moisture is also
responsible for control of dimensional properties of biscuit.
a. Moisture in flour from break passages
Moisture contents in the flour streams decreased gradually from the initial moisture 16%
(wheat) to 12.29% in flour. The moisture amount recorded in break rolls decreased from
15% to 12.29% that clearly indicated that the wheat flour fractions were losing moisture
during milling because of the heat generated by friction energy. The overall moisture loss
in break roll was 2.72% during milling from 1st to 5th break.
42
Figure 4: Variation in moisture (%) in flour from break streams.
b. Moisture in flour from semolina passages
The moisture was recorded as 13.14% in flour taken from coarse semolina whereas
12.26% to 12.94% moisture was observed in flour produced from three streams of fine
semolina. Total 0.68% decrease in moisture was observed in three streams of fine
semolina that was a negligible loss in moisture.
Figure 5: Variation in moisture (%) in flour from semolina streams.
c. Moisture in flour from semolina overtail passages
The moisture loss as 12.88% to 11.72% was recorded in these four streams. Lower
moisture content was evident in semolina overtail passages.
15.0114.47
13.7313.22
12.29
1st Break 2nd Break 3rd Break 4th Break 5th Break
13.14
12.9412.83
12.26
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
43
Figure 6: Variation in moisture (%) in flour from semolina overtail streams
d. Moisture in flour from middling passages
The decrease in moisture content was also observed in the flour streams of middling. C7A
and C7B were the streams found with very low moisture content even up to 11.7%. The
first three flour middling stream had higher moisture level (13.21%-13.87%) with a
difference of 0.66% while the last three streams had shown very low moisture level
(12.3% - 11.7%) with a difference of 2.17% from the highest moisture of middling stream
(13.87%).
Figure 7: Variation in moisture (%) in flour from middling streams
e. Conclusion
The percent moisture was decreasing as milling further proceeded i.e. the particle size
was reduced constantly (as mentioned in 3.1.3.1.7). Higher moisture contents were
observed in break streams whereas the flour from middling, overtail and semolina
12.88
11.72
12.02
12.39
C1B C4 C5 C6
13.47
13.87
13.21
11.84 11.70
12.30
D1 DD1 R1A C7A C7B C8
Moisture (%) in Flour Streams from Middling
44
streams showed similar values of moisture. Along with the recipe water, the moisture
already present in flour is very important in producing required dough (Wade et al, 2012).
3.1.3.1.2. Protein
The total proteins content include all types of proteins present in the flour (including the
gluten proteins). Since gluten plays the determining role in the evaluation of flour quality,
dough making and texture formation of biscuit, it is separately analyzed in the laboratory.
Total protein analysis is therefore not an only significant parameter to predict flour
behavior on production lines (Gaines et al, 2006; Fustier et al, 2009).
a. Protein content in flour from Break passages
Protein content was found to be increasing as the wheat kernel was getting milled,
10.23% protein was reported in the flour from 1st break whereas highest amount of
protein as 13.97% was observed in flour from 3rd break. Increase in protein was due to
the inclusion of bran that is a rich source of bran proteins.
Figure 8: Variation in protein (%) in flour from break rolls streams
b. Protein content in flour from Semolina passages
Quite consistent amount of protein was found to be present in 4 streams from semolina
(10% to 10.4%). Similar like gluten, the low protein content in flour is perfect for cookie
making in baking industry.
10.23
12.40
13.9713.33
12.60
1st Break 2nd Break 3rd Break 4th Break 5th Break
45
Figure 9: Variation in protein (%) in flour from semolina streams
c. Protein content in flour from Semolina overtail passages
Increase in protein content as 10.15% to 11.3% was recorded in overtail streams of
semolina due to the inclusion of bran. Bran proteins are widely distributed in pericarp.
Enough information is not yet available that whether bran protein behave as gluten
protein or they disturb the gluten network.
Figure 10: Variation in Protein (%) in flour from semolina overtail streams
d. Protein content in flour from Middling passages
The protein amount in middling streams varied widely. The minimum quantity of protein
as 9.6% was recorded in R1A stage/streams while maximum was found as 11.4% in C7B.
10.40
10.30
10.20
10.00
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
10.40
10.15
11.05
11.30
C1B C4 C5 C6
46
Figure 11: Distribution of protein (%) in flour from middling streams.
e. Conclusion
Consistency in protein distribution was recorded in semolina streams. Our results
confirmed the earlier findings that streams rich in ash contents were found also to have
high amount of protein. Protein and ash showed close association in compositional
distribution of protein in the wheat kernel.
3.1.3.1.3. Ash
Both the components of flour i.e. ash and proteins act as a deciding factors of flour quality
for biscuit, cake, crackers etc. The lower ash and protein content are the indicators for
soft quality of flour; hard and durum flours consist more protein. The increased amount
of protein and ash in the flour produces cookies of hard texture, reduced diameter and
darker in color.
a. Ash content in flour from Break passages
Constant increase in ash content was observed in streams obtained from break rolls
however the rate of increase was maximum in streams from 4th to 5th rolls. Minimum ash
content 0.63% recorded in 1st break whereas maximum ash % i.e. 1.38% was recorded in
5th break with a difference of 0.75%. The results showed that ash was found to be
increasing with further grinding of wheat, suggesting wheat bran was gradually being
finely ground and mixed in flour. Geng et al (2012) have also reported the ash enrichment
of flour in break streams in later phases of milling.
10.65
11.15
9.60
11.30 11.40
10.75
D1 DD1 R1A C7A C7B C8
Protein (%) in Flour Streams from Middling
47
Figure 12: Variation in ash (%) in flour from break rolls streams
b. Ash content in flour from Semolina passages
The amount of ash produced in semolina streams was found to be reduced. As the flour
passed through the purifiers, the bran was completely eliminated which was a rich source
of ash. The importance of measuring ash diversity is essential to assess the changes of
flour in quality during disintegration or the streams collected and its impact on spread
ratio of the cookies (Gaines et al, 1988).
Figure 13: Variation in Ash (%) in flour from semolina streams
c. Ash content in flour from Semolina Overtail passages
The ash obtained in the streams C1B, C4, C5 and C6, ranged from 0.35% to 0.7% which
were collected immediately after purifier stage and named as overtail (as they retained
on the sieves of purifier). The lower ash quantity in C1B and C4 was due to the removal
of bran flakes from sieves and less opportunity of bran to be finely ground by the set of
0.63 0.65
0.94
1.08
1.38
1st Break 2nd Break 3rd Break 4th Break 5th Break
0.41
0.35
0.39
0.42
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
48
rollers in initial stage. In later phases finely ground bran was mixed with flour thus
increased the ash value.
Figure 14: Ash (%) in flour Streams from semolina overtail streams
d. Ash content in flour from Middling passages
The ash contents present in streams in middling varied from 0.37% to 0.87% with a
difference of 0.50%. The flour consisting high ash content is usually directed towards Atta
(a low refined type of flour used for Chapatti making in Pakistan), whereas low ash flour
is mixed with flour used for biscuit production. The flour from middling streams showed
very varied ash distribution as also shown in the case of moisture distribution.
Figure 15: Variation in ash (%) in flour from middling streams
0.35
0.44
0.660.70
C1B C4 C5 C6
0.49
0.62
0.37
0.78
0.87
0.65
D1 DD1 R1A C7A C7B C8
49
e. Conclusion
The flour consisting low ash were produced from all the streams in middling and
semolina. Wide variation was noticed in all type of streams. The lower ash content in
flour streams from middling and semolina showed that they should be included more in
blending for biscuit making and ratio should be adjusted accordingly.
3.1.3.1.4. Gluten index
GI is a parameter in flour that predicts the dough strength based on network making
ability during dough formation. High GI reflects strong network of gluten proteins present
in the flour. The flour suitable for biscuit production should make weak gluten network
i.e. low GI. (Madugiri et al 2008) as dough required to be soft in nature.
a. Gluten Index in flour from Break passages
High value of GI was observed that varied from 88 to 96, strong gluten network is
expected from all the break roller streams. However a constant increase or decrease in
GI was not observed.
Figure 16: Variation in gluten Index (%) in flour from break streams
b. Gluten Index in flour from Semolina passages
The semolina flour showed slightly less GI values from 83 to 95. It was an indication that
purified flour was producing slightly less glutenins as compared to gliadins.
93
88
93
96 96
1st Break 2nd Break 3rd Break 4th Break 5th Break
50
Figure 17: Variation in gluten index (%) in flour from semolina streams.
c. Gluten Index in flour from Semolina overtail passages
Minimum GI achieved in C4 passages, the reason is unknown but it may be attributed to
low ash content.
Figure 18: Variation in gluten index (%) in flour from semolina overtail streams.
d. Gluten Index in flour from Middling passages
Variation showed decrease in gluten index in flour streams from 93 to 84, almost a
constant decline.
87
95
83
94
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
94
70
9288
C1B C4 C5 C6
51
Figure 19: Variation in gluten index (%) in flour from middling streams.
e. Conclusion.
Slight higher GI was observed in all the streams however, the streams also had low ash
content, it was looked that the medium GI and low ash complement each other and the
flour was suitable for biscuit making.
3.1.3.1.5. Dry Gluten
Generally flour is categorized on the basis of dry gluten content. Higher dry gluten values
referring to hard flour are required for pasta, pizza and bread making whereas low dry
gluten values is desired for biscuit, wafers and cakes.
a. Dry gluten in flour from Break passages
The dry gluten varying from 6.9% to 10.03% was obtained in 5 break rolls. However the
quantity of dry gluten rose till the streams obtained from 3rd break then it dropped in the
4th and 5th break. The rise and fall in the quantity of dry gluten probably was related to
the design and number of the grooves present in each roller.
93
92
9091
88
84
D1 DD1 R1A C7A C7B C8
52
Figure 20: Variation in dry gluten (%) in flour from break rolls streams
b. Dry gluten in flour from Semolina passages
The dry gluten recorded in semolina varied from 7.3% to 8.8% with a difference of 1.5%.
No significant difference or relation was observed. The difference in gluten content in
different streams might be linked with the gap between the two rollers and its differential
speed.
Figure 21: Variation in dry gluten (%) in flour from semolina streams
c. Dry gluten in flour from Semolina overtail passages
The dry gluten in flour was recorded the higher values varied from 8.7% to 9.4% with a
maximum difference of 0.7%. There are many number of factors that may influence the
inclusion of gluten in flour (endosperm) such as the distance between the roller, design
etc.
7.43
9.6010.03
7.20 6.90
1st Break 2nd Break 3rd Break 4th Break 5th Break
7.90
8.80 8.60
7.30
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
53
Figure 22: Variation in dry gluten (%) in flour from semolina overtail streams.
d. Dry gluten in flour from Middling passages
All variety of flours consisting variable quantity of DG obtained from 6 middling streams
showed different percentage of dry gluten in initial, middle and the last streams. The
quantity of DG varied from 7.00% to 9.8% with a difference of 1.8%.
Figure 23: Variation in dry gluten (%) in flour from middling streams.
e. Conclusion
The quantity of dry glutens obtained from various streams varied widely as recorded in
flour collection. A strong relation of ash with dry gluten was observed in break roll
streams as the values of ash as well as dry gluten were found to be the highest. It may be
attributed to the fact that minerals generally are bound to the proteins. It may be pointed
out here that how higher values of dry gluten are helpful to categories flour as weak,
strong or durum.
8.70
9.25
9.40
9.20
C1B C4 C5 C6
8.35 8.40
7.00
9.60 9.80
8.50
D1 DD1 R1A C7A C7B C8
54
3.1.3.1.6. Wet Gluten
The wet gluten is similar in parameter to DG that is used to identify the flour type,
strength based on the gluten proteins network. Most of the flour standards are based on
gluten contents where gluten is referred as wet gluten. It also predicts the water
absorption capabilities of gluten which is linked to end quality of most of the baked
products. The water absorption value obtained from Farinograph represents the water
retained by all the hydrophilic components present in flour including the water held by
the gluten proteins.
There was no significant variations in values as observed in analyzing various streams.
Figure 24: Variation wet gluten (%) in flour streams from 18.8 to 28.78%.
Figure 25: Showing minor variation in wet gluten (%) in flour streams from 20.70 to
26.1
22.02
28.27 28.78
20.4618.80
1st Break 2nd Break 3rd Break 4th Break 5th Break
Wet Gluten (%) in Flour Streams from Break Rolls
23.7526.10 25.95
20.70
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
Wet Gluten (%) in Flour Streams from Semolina
55
Figure 26: Variation in wet gluten (%) in flour streams from 25.75 to 29.23
Figure 27: Wet gluten (%) in Flour streams from middling
3.1.3.1.7. Particle size distribution
Particle size of flour plays vital role in determining the water absorption, damaged starch
production, and evaluation of the texture of the biscuit.
a. Particle size in flour from Break passages
The present milling design produced flour of particle size 132 micron from 1st and 2nd
break, whereas the flour from 3rd, 4th and 5th break maintained as 180 micron. The
retention of flour particles at 160 micron sieve including the sieve 1st and 2nd was almost
nil, whereas the particle size of the flour from 3rd, 4th, and 5th break rolls was increasing.
At 125 micron, highest retention was observed in 4th break. Whereas lowest retention
was observed in 1st break. Overall, very fine particle of flour was produced by 1st and 2nd
break, whereas 4th break produced flour of coarse particle.
25.75
28.9529.23
27.33
C1B C4 C5 C6
Wet Gluten (%) in Flour Streams from Semolina overtail
25.58 25.53
21.50
28.5030.05
26.08
D1 DD1 R1A C7A C7B C8
56
Figure 28: Showing increase in % retention at 160 µm sieve of flour streams from
break rolls
Figure 29: % Retention at 125 µm sieve of Flour streams from break rolls
Figure 30: % through from 125 µm sieve of Flour streams from break rolls
0.1 0.7
33.0
38.8
46.8
1st Break 2nd Break 3rd Break 4th Break 5th Break
6.7
13.3
37.7
43.6
30.1
1st Break 2nd Break 3rd Break 4th Break 5th Break
93.286.0
29.3
17.623.1
1st Break 2nd Break 3rd Break 4th Break 5th Break
57
b. Particle size in flour from Semolina passages,
A fine semolina passage C2C, 180 micron sieve was placed due to which high relation at
160 micron observed. C2C produced coarse particle flour whereas C3A, C2A/B produced
very fine flour.
Figure 31: % Retention at 160 µm sieve of flour streams from semolina showing
retention 0.1 to 9.1%
Figure 32: % of flour streams retained at 125 µm sieve from 5.0 to 72.8% in semolina
passages
2.6
9.1
0.2 0.1
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
6.9
72.8
25.1
5.0
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
58
Figure 33: % of flour streams from semolina from 125 µm sieve.
c. Particle size in flour from Semolina overtail passages
Fine flour retained at 125 micron in C5 and C6 is to be higher than the flour that passed
through the sieve. Whereas a small amount of coarser flour was retained in C1b and C4.
Figure 34: % of Flour Streams from 0.1 to 4 retained at 160 µm sieve in semolina
overtail passages
90.5
18.1
74.8
94.9
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
4.0
0.1 0.2 0.1
C1B C4 C5 C6
59
Figure 35: % Retention at 125 µm sieve of flour streams from semolina overtail
Figure 36: % through from 125 µm sieve of flour streams from semolina overtail
d. Particle size in flour from Middling passages
The streams R1A, C7A, C7B and C8 produced fine particle size flour whereas DD1
produced coarse flour.
54.7
43.1
7.9
20.9
C1B C4 C5 C6
41.3
56.9
92.0
79.0
C1B C4 C5 C6
0.6
12.8
0.80.1 0.1 0.3
D1 DD1 R1A C7A C7B C8
60
Figure 37: % Retention at 160 µm sieve of flour streams from middling
Figure 38: % Retention at 125 µm sieve of flour streams from middling
Figure 39: % through from 125 µm sieve of flour streams from middling
e. Conclusion
Different fractions of flour consisting different particle size are received during milling by
setting the distance between the rollers and using sieves of different sizes
As per customer requirement the flour of a particular particle size may be obtained by
applying modification in milling techniques and using specified blending techniques to
produce the composite flour.
18.5
29.4
20.8
10.9
19.0
12.8
D1 DD1 R1A C7A C7B C8
81.0
57.8
78.4
89.0
80.986.9
D1 DD1 R1A C7A C7B C8
61
3.1.3.2. Study of the Dough Rheology of Flour – Farinograph Analysis
Dough behavior during mixing is determined by using variety of chemical and
instrumental methods, Farinograph is one of them. Following parameters from
Farinograph were helpful in understanding the dough development process.
3.1.3.2.1. FQN
Farinograph quality number is known to predict overall behavior of flour, higher values
represents the hard flour. The Farinograph quality number is directly linked to the
dimensional properties of biscuit such as the high FQN will give low spread ratio of the
biscuit.
a. FQN in flour from Break rolls milling passages
Very high FQN was reported in streams from break roll except on 1st break where only 23
FQN was received. The streams from other break passages showed and confirmed the
production of hard flour and provided strong dough making ability of flour.
Figure 40: FQN in flour from break streams
b. FQN in flour from Semolina passages
Almost every stream showed softness in dough except the fine semolina C2C. FQN values
i.e. 25, 26 and 27 were reported in C1A, C2A/B and C3A respectively. It stated that
semolina streams produced flour of low FQN in comparison with flour from break rolls.
Low FQN in semolina streams suggesting that softest flour was achieved in pure
23
155 154
122110
1st Break 2nd Break 3rd Break 4th Break 5th Break
62
endosperm part of the wheat grain or might be low ash content contributed to the
softness with respect to the FQN value.
Figure 41: FQN in Flour from semolina streams
c. FQN in flour from Semolina overtail passages
Very low FQN in C1B was reported. It is a first stream of semolina overtail of purifier. Rest
of the streams were produced middle range of FQN around 67 to 74.
Figure 42: FQN in Flour rom semolina overtail streams
d. FQN in flour from Middling passages
Low (22) to high (100) FQN were observed in middling passages. Half of streams
contained FQN in lower side whereas FQN was increased as grinding proceeded.
25
98
27 26
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
9
67
74 74
C1B C4 C5 C6
63
Figure 43: FQN in flour from middling streams
e. Conclusion:
High FQN flour was produced in break stages whereas low FQN was produced by
semolina streams.
3.1.3.2.2. Water absorption
It is an important parameter in dough making process suggesting changes in flour
behavior. High WA% is required in pasta and bread making process whereas low WA% is
the required for biscuit and cake. The WA is closely associated to ash and damaged starch
present in the flour.
a. Water absorption in flour from Break rolls passages
Water absorption was increasing as wheat was further ground. Very low water
absorption was the result of having low content of damaged starch, protein and ash
content in the flour streams. The WA was gradually increased in 5th break from 53.2% to
66.6%. However a constant increase in water absorption was observed.
27 2922
88
100
47
D1 DD1 R1A C7A C7B C8
64
Figure 44: Water absorption % in Flour from break streams
b. Water absorption in flour from Semolina passages
The percent of water absorption was ranged from 58.6% to 69%, while the lowest value
in stream of break roll which was 53.2% while in semolina streams it was recorded as
62.2% for the first stage passage (coarse semolina). In fine semolina passages, WA was
reported as 58.6% which then increased up to 67% in further streams. It had clearly
shown that in further processing, flour was getting damaged and would take extra water
in recipe.
Figure 45: Water absorption % in Flour from semolina streams
c. Water absorption in flour from Semolina overtail passages
The stream C1B had low WA as 57% whereas all the overtail streams of semolina had
high WA ranged from 64.8% to 68.3%. The water absorption increased slightly from the
53.256.0
60.162.6
66.6
1st Break 2nd Break 3rd Break 4th Break 5th Break
62.2
58.6
62.4
67.0
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
65
water absorption in break roll and semolina streams, which showed highest values as
66.6% and 67% respectively.
Figure 46: Water absorption % in flour from semolina overtail streams
d. Water absorption in flour from Middling passages
The amount of WA fluctuated within the range of 59.2% to 67.9%. The streams in the
initial stage had low water absorption, however WA raised in the central streams and last
i.e. C8, it again dropped to 59.2%.
Figure 47: Water Absorption % in flour from middling streams
e. Conclusion
The highest and lowest value of WA in streams from break roll, semolina, semolina
overtail and middling recorded as 53.2-66.6%, 58.6-67%, 57-68.3% and 59.2-67.9 %
57.0
68.3
66.064.8
C1B C4 C5 C6
Water Absorption % in Flour Streams from Semolina overtail
60.4
59.2
67.066.1
67.9
63.2
D1 DD1 R1A C7A C7B C8
66
respectively showed an overall increase of 6% from lowest value while an increase of 1-
2% in highest absorption value.
3.1.3.2.3. Dough development time
The dough development time depends on the nature of hardness of the flour, especially
the amount of hydrophilic components of flour. The hydrophilic biopolymers present in
flour include starch bran, proteins and pentosan. The hydration capacity and hydration
rate of the flour are associated with these components. DDT is an indicator that how
much time is required for a flour to form a desired dough. Higher DDT represents the
hard flours and need more water to be absorbed.
a. Dough Development time in flour from Break Rolls passages
Initial two break rolls streams produced low DDT whereas following three streams
required longer time for dough to develop DDT. It might be attributed due to the
inclusion of bran that showed high water absorption.
Figure 48: DDT (min) in flour from break rolls streams
b. Dough Development time in flour from Semolina
The low DDT of 1.5 to 1.9 min was reported in semolina streams. Dough would be
developed early if flour from these streams are to be utilized in biscuit making and saving
of energy required in mixing i.e. cost involved will be reduced.
1.3
2.5
7.1
5.5 5.7
1st Break 2nd Break 3rd Break 4th Break 5th Break
67
Figure 49: DDT (min) in flour from semolina streams
c. Dough Development time in flour from Semolina overtail passages
The C5 passage produced high DDT i.e. 12.9 minutes where as others produced lower
DDT values. Reason for C5 to take longer dough mixing time might be attributed to
distance of rollers in this portion, change in sifter or other reasons for variation in particle
size. However it showed that the flour from C5 should either be recycled or mixed with
semolina or middling streams in the appropriate proportion to suit end quality and to
reduce DDT.
Figure 50: DDT (min) in flour from semolina overtail streams
d. Dough Development time in flour from Middling passages
The dough development time remained almost constant and streams were consistent in
terms of DDT recorded in middling streams. The time for development of dough was the
least i.e. only 1.5 to 1.7 minutes in middling streams.
1.5
1.7 1.7
1.9
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
1.7 2.0
12.9
1.9
C1B C4 C5 C6
68
Figure 51: DDT (min) in flour from middling streams
e. Conclusion
Although not very strong relationship of DDT was found with any other parameter, but
as some association has been found with ash, water absorption and particle size of the
flour, the collective values of the above parameters will reduce the mixing time.
3.1.3.2.4. Dough Stability (DST)
The strength of dough to remain stable is expressed as dough stability, it indicates that
how much a flour after conversion to dough during continuous mixing may hold its
network in native form and prevent the dough from turning to be more fluid. The high
DST represent strong dough made from hard flour. The network holding property against
mechanical shearing if gets prolonged dough will produce an optimal dough.
a. Dough Stability in flour from Break passages
Flour streams in first break produced less stable flour whereas second and third break
produced flour that made highly stable dough. Flour of medium stability was also
achieved. The dough stability was highest as 14.7 min in the 3rd break streams and lowest
1.9 min in the 1st break with a difference of 12.8 min while the average time for the dough
to remain stable was noted as approx. 9.4 min.
1.6 1.6
1.5
1.7 1.7 1.7
D1 DD1 R1A C7A C7B C8
69
Figure 52: DST (min) in flour from break streams
b. Dough Stability in flour from Semolina passages
Very low to medium DST was achieved at this stage ranging from 0.9min to 8.6 min with
and average of 3.8 min. showing that flour needs to be mixed with flour of high DST if
long duration of mixing is required before baking.
Figure 53: DS (min) in flour from semolina streams
c. Dough Stability in flour from Semolina overtail passages
Medium DST was achieved in these streams, values varies from 5.3 min to 8.4 min. The
difference in dough stability among the four stream was less (3 min) as compared to the
stability of other streams 8.3 min.
1.9
13.614.7
9.5
7.5
1st Break 2nd Break 3rd Break 4th Break 5th Break
1.3
8.6
4.5
0.9
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
70
Figure 54: DST (min) in flour from semolina overtail streams
d. Dough Stability in flour from Middling passages
The dough was found to be stable for only a short period of time i.e. for two minutes or
even less in first three streams of middling, later on it remained stable up to 7.7 minutes.
The stability time of dough varies from 1 min to approximately 8 min in various streams
of middling.
Figure 55: DST (min) in flour from middling streams
e. Conclusion
DST was decreasing as ash, particle size, protein and damaged starch were increasing in
the flour. The dough stability time is highly important in control of the process, because
of DST is more than the time required for sheeting, cutting and time taken just before
entering in the oven, than end quality of biscuits will not change throughout baking,
otherwise the last batch of biscuits will be of poor quality.
8.3
7.5
8.4
5.3
C1B C4 C5 C6
1.9 2.1
0.6
6.9
7.7
3.9
D1 DD1 R1A C7A C7B C8
71
3.1.3.2.5. Degree of softening DoS (ICC)
Dough rheology change rapidly during mixing. The DoS after 10 minutes of mixing time
or 12 minutes give certain characteristics of dough related to end quality. It determines
the softness in dough structure that is also visible in SEM microstructure. The value of
higher DoS reflects soft dough, suitable for production of biscuit, cake etc.
a. Degree of softening in flour from Break passages
The DoS in break streams fluctuated widely and did not show any distinct relationship
and as the value range from 23.3 to 71 FU (Farinograph Unit).
Figure 56: DoS (FU) in flour from break streams
b. Degree of softening in flour from Semolina passages
The flour streams from semolina showed that dough prepared from Semolina flours
would have a softer structure than dough processed from flour stream from break roll.
The range (48 FU to 96 FU) as found in the Semolina flour. The DoS between 48 to 96 FU
is suitable for biscuit and cookie.
71.3
27.0
45.0
23.3
60.0
1st Break 2nd Break 3rd Break 4th Break 5th Break
72
Figure 57: DoS (FU) in flour from semolina streams
c. Degree of softening in flour from Semolina overtail passages
Mid-range of DoS (47 to 69 FU) was reported in these streams. The difference of 22 FU
was quite distinct and wide, however it was less than the same difference in FU was
observed in streams from break and semolina.
Figure 58: DoS (FU) in Flour from semolina overtail streams
d. Degree of softening in flour from Middling passages
R1A was found softest among all the streams which produced DoS value as 137,
otherwise mid-range of DoS was reported in the remaining streams.
74.0
48.0
62.5
96.0
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
54.0
69.0
47.049.5
C1B C4 C5 C6
73
Figure 59: DoS (FU) in flour from middling streams
e. Conclusion
Summary of the Farinograph parameters, In general, flour from break rolls were found
to produce soft nature dough. The Farinograph parameters are very helpful in evaluating
the precautions to be taken during mixing to get optimal dough which behaves without
problem in processing.
3.1.3.3. Pasting Behavior of Dough – MVAG
3.1.3.3.1. Maximum hot paste viscosity/Peak viscosity (MV/PV)
Both the MV and PV values are referred in the literature for describing the maximum hot
paste viscosity, however in the present description only MV is used to avoid any
confusion. The flour having high maximum/peak viscosity tends to have high swelling
ability. They can hold high moisture under critical temperature and mechanical strength.
In general soft wheat flours show highest MV as compared to hard flours or durum. The
highest pasting viscosity indicated the high content of starch in wheat flour.
a. Peak/Max. viscosity in flour from Break passages
The MV/PV was found to be decreasing constantly as grinding further proceeded. The
MV as 996 BU was recorded as the highest value of maximum viscosity observed in the
1st break. The slight decrease in max viscosity in later stages may be due to a constant
increase in damaged starch content. The lowest MV as 814 BU was observed in the 5th
break with a difference of 182 BU.
76.0
53.0
137.0
53.0 49.0
72.5
D1 DD1 R1A C7A C7B C8
74
Figure 60: Max. Viscosity (BU) in flour from break streams
b. Peak/Max. viscosity in flour from Semolina passages
It was observed that among the semolina streams maximum viscosities increased from
860 to 1047 BU with a difference of 187 BU although the increase was not constant and
both the fine and coarse streams showed varied value of MV.
Figure 61: Max. Viscosity (BU) in flour from semolina streams
c. Peak viscosity/Max. in flour from Semolina overtail passages
The C4 passage produced the least maximum viscosity of 875 BU, whereas high viscosities
were recorded in rest of the passages. The highest value recorded as 1047 BU was
observed in only either the streams Semolina or Semolina overtail.
996.0947.0 918.0
867.3814.0
1st Break 2nd Break 3rd Break 4th Break 5th Break
958.01047.0 1031.0
860.0
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
75
Figure 62: Max. Viscosity (BU) in flour from semolina overtail streams
d. Peak/Max. viscosity in flour from Middling passages
R1A had the low maximum/peak viscosity, whereas high viscosities were achieved by rest
of the streams. The lower value of MV was recorded in 5th break as 814 BU, in semolina
as 860 BU, in semolina overtail as 875 BU and in middling streams as 848 BU.
Figure 63: Max. Viscosity (BU) in flour from middling streams
3.1.3.3.2. Break Down viscosity (BDV)
The BDV is correlated to the trough viscosity which is also referred as the minimum hot
paste viscosity. The difference between the maximum hot paste viscosity (MV or PV) and
the minimum hot paste viscosity (trough viscosity) is referred as BDV and is calculated
from a pasting curve. The starch granule in the grains get disrupt during holding period
of the viscosity test because the starch is subjected to mechanical shear stress , amylose
to leach out and re arrange itself. This period is closely associated to BDV. Various
1047.0
875.0
1011.5993.5
C1B C4 C5 C6
989.51032.5
848.0
966.0 969.0 959.5
D1 DD1 R1A C7A C7B C8
76
starches behave differently to be stable at this high temperature and shear and are
related to dough spreading during baking. The swelling of starch granules during baking
or heating is related to high value of BDV and MV. Both MV and BDV are associated with
the end quality i.e. puffing and spreading.
a. Break Down viscosity in flour from Break passages
Similarly like MV, BV was also found to be decreasing in break roll streams from 1st break
to the 5th break roll stream. The highest BV was recorded in 1st break as 355.7 BU whereas
lowest recorded in the 5th break as 295 BU, with a difference of 60 BU.
Figure 64: BD Viscosity (BU) in flour from break streams
b. Break Down viscosity in flour from Semolina passages
The breakdown or the BDV values reported in semolina stage varied from 326 BU to
383.5BU with a difference of 59 BU. So maximum value of 355BU from the first break roll
streams was almost maintained in the flour stream from Semolina. The highest value of
385.5 BU in Fine C2A/B was recorded against the lowest value of 326 BU.
355.7335.7
353.3324.5
295.0
1st Break 2nd Break 3rd Break 4th Break 5th Break
77
Figure 65: BD Viscosity (BU) in flour from semolina streams
c. Break Down viscosity in flour from Overtail passages
The breakdown viscosity record showed a difference of 57.5BU. Lowest BD was reported
in C4 i.e. 186BU. Highest reported in C5. The difference in BDV in the semolina overtail
stream was recorded as the highest 204.5BU. This property may be attributed to highest
particle size of the flour.
Figure 66: BD Viscosity (BU) in flour from semolina overtail streams
d. Break Down viscosity in flour from Middling passages
High BDV was reported in all the middling stage streams with minor difference in values.
The highest BDV of 386.0 BU is obtained from Stream DD1 while the stream R1A gave the
lowest value as 308 BU, the difference of only 78 BU.
358.0
370.0
383.5
326.0
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
385.0
186.0
390.5 377.5
C1B C4 C5 C6
78
Figure 67: BD Viscosity (BU) in flour from middling streams
3.1.3.3.3. Setback viscosity (SV)
As the BDV is related to behavior of Starch during heating the setback viscosity is the
change in viscosity during cooling and is calculated from pasting curve obtained from
MVAG by subtracting the trough viscosity from final viscosity FV. The final viscosity
represents the viscosity at the end for the test after cooling the paste to 50 0C and holding
the paste at the temperature. The trough viscosity (not mentioned in the present
discussion but shown on pasting curve) is related to holding strength of the paste. The SV
is associated to Starch molecules especially amylose re arrangement during cooling to
form gel structure in dough. FV therefore rises during cooling due to retro gradation of
starch. If the rate of retro gradation of starch will be high, high value of SV will be
recorded. The low SV indicates soft flour.
a. Setback viscosity in flour from Break passages
An increasing trend of SV was observed. 402.3 to 568.7 BU was the range observed in
break streams. Highest viscosity was recorded in 1st break. The first break stream had the
highest SBV as 568.7 BU as compared to the lowest SBV of 402.3 BU from the 4th beak
stream with a difference of 166.4 BU.
369.5386.0
308.0
378.0 383.0368.0
D1 DD1 R1A C7A C7B C8
79
Figure 68: SB Viscosity (BU) in flour from break streams
b. Setback viscosity in flour from Semolina passages
The streams from Semolina did not show significant difference in SB values as compared
to the values form Break rolls. The mid-range of SB was observed in the semolina stage.
Figure 69: SB Viscosity (BU) in flour from semolina streams
c. Setback viscosity in flour from Overtail passages
A great variation in SBV was observed in the streams from Semolina overtail as 298.5 BU
as the minimum setback viscosity recorded in semolina overtail of C4. While the highest
SB viscosity 578 BU was observed in Fine C2C with a difference of 268.5 BU.
568.7531.7
508.0
402.3
452.0
1st Break 2nd Break 3rd Break 4th Break 5th Break
496.0
578.0537.0
467.0
Coarse - C1A Fine - C2C Fine - C2A/B Fine - C3A
80
Figure 70: SB Viscosity (BU) in flour from semolina overtail streams
d. Setback viscosity in flour from Middling passages
The minimum SB viscosity as 465 BU whereas high SB viscosity as 547.5 BU were recorded
in middling stage and a difference of only 82.5 BU.
Figure 71: SB Viscosity (BU) in flour from middling streams
e. Conclusion:
The various viscosities i.e. MV, BDV and SBV indicated pasting properties (from the
pasting curve) clearly of the behavior of flour during heating and cooling process. The
study of the pasting curve or more elaborating the viscosities value (MV, BDV, and SBV)
would be very helpful in selection of streams and their inclusion for a particular bakery
product.
567.0
298.5
530.0 512.5
C1B C4 C5 C6
531.5
547.5
465.0
478.0
506.0
521.0
D1 DD1 R1A C7A C7B C8
81
3.1.3.4. Solvent Retention Capacity of Flour Streams
The SRC test is a sum of flour test i.e. SC-SRC, Water SRC, Su-SRC and LA-SRC, indicating
the presence of different components of wheat flour.