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    Manufacturing of Ethyl Alcohol from Fruit Waste

    INTRODUCTION

    In general, alcohol means colorless volatile inflammable liquid especially

    intoxicant in wire, beer, spirits etc. and as a solvent, fuel etc. Depending on the

    interest of the person involved, for alcohols are many things to many people. To

    most non technical people, "alcohol" in the broad sense is used to describe any

    intoxicating beverage; thus, a heavy or habitual drinker is called "alcoholic" the case

    is some what different in the industrial manufacturing fields which produce finished

    goods, intermediates, or raw materials, alcohols play a key role as important

    organic solvents and rank second only to water in terms of their almost universal

    application. Hence to these people alcohols mean solvents.

    Take a spoonful of medicine; feel the smoothness of the lacquer on the pine

    pralines in the play room ; look at the tyres of your car, smell the window cleaner

    spray, make use of a hair spray, deodorant stick, or are antiperspiral; carry your

    water proof cloth covered books to school etc. Alcohols play their solvent role in all

    these personal events. Alcohols can be regarded as hydroxyl derivatives of

    hydrocarbons, one the basis of several types of classification, di-hydric. There are

    various types of alcohol belonging to the homologues series of alcohols, of like

    methanol, ethanol, propanol etc. teach member in the series have its own specificproperty and most active member of the series is "Ethanol".

    Here the fig. Below shows the chemicals from ethanol.

    C.O.E.& T.,Akola 1

    Acetaldehyde

    Ethylene

    AlkylatedAeromatics

    Diethyl Ether

    Mixed ether

    Organic Esters

    ButadieneEthoxides

    Halides

    Esters

    Ethanol

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    distillation came into the mind of the people workers over the put of alcohol for

    India.

    In India, the concept of fermentation was commercialized in 1900 to 1910

    after the discovery of Louis Pastern and the process came in to use before 1930 to

    about 1948 saw the development of indirect Hydration process to manufacture

    Ethanol synthetically.

    OBJECTIVE :

    Growth in potable alcohol industries in liked with the demand for the

    consumption of the people and the chemical products in industries in which alcohol

    plays an impatant role.

    Fruits ripe within 4-5 days, the unripe fruits can be stored at 50% 52 F forfive weeks while ripe fruits can be stored at 320 to 350F.

    Yield up to 10 years 750 fruits/ha.

    Field up to 5 years 1000 1500 fruits/ha.

    After 15 years, yield was 2000 2500 fruits or 18 20 tons /ha.

    Especially, in Maharashtra, Sapota was grown in area of 3900ha and the

    production was obtained 10,920.

    HANDLING AND STORAGE :

    Unripe Sapota is kept into the large capacity containers and the containers

    are packed with the straw. So, that the surface of the two fruits could not touch with

    each other. It should be stored away from all ignition sources and also from high

    and low temp. The temp is kept moderate ( depending upon the atmosphere

    conditions of the place ).

    Under these conditions, the unripe Sapota gets ripen and ready to eat.

    All the sources for ethanol production

    The three types of sources of ethanol production

    1) SACCHARINE ( Sugar containing ) materials in which the carbohydrate ( the

    actual substance from which the alcohol is made ) is present in the form of simple,

    directly fermentable six and twelve carbon sugar cane, sugar beets, fruit ( Fresh or

    dried ), citrus molasses, cane sorghum why and skim milk.

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    2) STARCHY MATERIALS : That contain more complex carbohydrates such as

    starch and insulin that can be broken down into the simplex sex and twelve carbon

    sugars by hydrolysis with acid or by the action of enzymes in a process called

    malting. Such materials includes corn, grain sorghum, barley, wheat, potatoes,

    sweet potatoes, Jerusalem artichokes, cacti manioc, arrowroot and so in.

    3) CELLULOSE MATERIALS :- Such as wood, wood waste, paper, straw, corn

    stalks, corn cobs, cotton, etc. which contain material that can be hydrolyzed with

    acid, enzymes or otherwise converted into fermentable sugars called glucose.

    Different type of fruits likely to produce ethanol.

    Fruit composition in Municipal solid waste :-

    The fruit pertaining to solid.The Municipal solid waste pertaining to fruit waste in Akola City is 25%.

    Now, the composition of waste, in Hampshire waste the energy content

    cones from :

    Articles % total of energy content

    Paper/Card 46%

    Plastics 22%

    Putrescibles 11%

    Fires 5%

    Textiles 3%

    Misc. 13%

    Table for carbohydrate content in other fruits.

    Fruit production and Acreage in Maharashtra :

    The fruit production and acreage in Maharashtra State is given below in table form

    as.

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    FRUIT CHOSEN FOR EXPERIMENTATION

    We have chosen the Chiku for experimentation. Botanical Name of Chiku is

    Acharas sapota and the Family name is Mallinkara acaracs.

    Chiku is called sapota. It is cheafly grown in moist coastal tracts of

    paninsular India, but in recent years it has spread in zones of the Deccan Plateau

    and also in sub mountain tracts of North India. In India the main centers of its

    cultivation are coastal tract and Maharashtra, coastal areas of Andhra Pradesh,

    Tamil Nadu, Karnataka, Saurashtra and sub-mountain areas of U.P. and Bengal. In

    Maharashtra it is grown over the area of 100 hectares mainly concentrated in

    Thana, Poona, Ahmednagar and Aurangabad districts. More than 70% of the area

    is is in Thana district. In India, it is mainly grown for fruits, but in other countries themilky latex from the bark of the tree yields an important commercial product, which

    forms the base for manufacture of Chewing-gum. It has very attractive shape and

    used as decorative tree.

    Origin:- It is a native of Maxico in Tropica, America, like that of guava. It is so

    established in India, that one can hardly believe that it is foreign to India.

    Tree characters:- It is slow growing evergreen tree, forms a good grown does not

    require any training and pruning, height of the tree is 8-12 m bears terminaly.

    Climate:- It is a tropical fruit crop which likes strictly tropical climate warm and moist

    weather with high annual rainfall of 250 cms (80"-100"). It thrives in places where

    maximum and minimum temperatures do not go beyond 340C and 110C. It does not

    very hot and dry summers and temperature below 50C. If temperature go above

    430C. dropping of blossom and scortching of fruits takes place in dry zones. Rain

    cloudy weather is not any way harmful to the plant. It can be grown from sea level

    to an elevation of 1000 m, but does not do well above 500 m. The best chiku

    plantations are found within a short distance from sea shore ( in heavy rainfall area).

    It can also be grown in drier tracts, chiku flowers all the year round in June-July,

    Oct-Nov, and Jan.Feb. While under Poona conditions it flowers in June-July and

    crops harvested in Dec-January.

    Soil :- Chiku can be grown in soils having a minimum depth of 1 m. having water

    table below 3-4 m. Chiku requires wall drained soils, alluvial loams on the river

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    banks, sandy loans sea, red lateritic soils of high rainfall area and well drained

    medium black soils are suitable for its cultivation. Chiku will not thrife well on ill

    drained soils, soils having hard pan below, loamy soils very deep and stickly soils,

    soils containing high per cent of lime are not suitable. The pH range should be 5.5

    to 7.5.

    Propagation:- Chiku is commercially propagated by vegetative methods like are

    layering or inarch grafting, Inarch grafts are prepared on the root stock seedlings of

    Rayans(Khirni) or chiku itself. In India, Khirni is very commonly used as root stock

    for chiku. The gooti is shallow rooted the majority of roots concentrating in upper

    30-40 cms. Of soils while roots of graft go as deep as 90 cms so gooti can thrive

    well in both light and deep soils while grafts are suitable for planting only in soilshaving 1 m depth, gooti is reported to hear sweeter and mellower pulp, Grafts on

    Khirni bear havily than on layers.

    Planting:- In drier part planting is done on the onset of monsoon where as in heavy

    rainfall areas it is planted after the heavy showers are over. Before planting the

    land should be ploughed harrowed and brought to a fine tilth. The pits of size 1 x 1

    x 1 m. are opened at a distance of 10 x 10 m. or 12 x 12 m. The pits should be

    filled in with 2 kg phosphate, FYM and good soil. After planting the plant should be

    supported with bamboo.

    Varieties:- There are three main varieties grown in Maharashtra.

    1. Kalipatti:- Leaves are dark green, leading variety of the state level shaped fruits,

    or excedant spreading branches. The quality is best, pulp is very sweet, mellowing,

    yields heavily. It contains one-two seeds, does well in climate of Konkan.

    2. Pillipatti:- Next best variety of the State. It is also called as 'Chatri' due to

    peculiar habit of growth in whorls, leaves lighter green, fruits are oval and round

    small fruits. It is less sweet as compared to Kalipatti. Does best in humid climate.

    3.Cricket ball :- Fruits large sized, round variety having granular flesh of market

    sweetness grown away from the see coast in drier areas. Bears heavily as

    compared to above two varieties.

    Manuring:- When the plants are one year old it should receive about 5 kg of FYM

    and about 150 gm of nitrogen. The doses should be increased with the

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    advancement in age. At the age of 7th years it starts bearing fruits. There are two

    main seasons Oct-Nov. and Jan-Feb, so far each flowering the tree should receive

    50 kg FYM + 1 kg N, 0.5 kg P2O5 and 0.5 kg of K2O. In drier areas the flowering will

    be mostly at beginning of monsoon, so manuring should be done in the month of

    May. In case of Chiku there is not bahar treatment (i.e. with holding of water

    practices are followed ). However, immediately after harvest orchard hygienic

    practices are followed.

    Training and Pruning:- Naturally chiku trees assumes a very attractive shape. It is

    an ever green tree and requires hardly and pruning, training is done by allowing the

    plant to grow upto and height of 1 m above which 3-4 well spaced branches are

    allowed to arise.Harvesting and Yield:- Fruits are ready for harvest in about 4 months i.e. Oct-Nov.

    flowering fruits matures by Jan-Feb. or flower matures fruits by April-May.

    Harvesting is done when fruits is fully developed matured fruit are not allowed to

    ripe on the fruit. At maturity it develop deep chocolate color. If you take a streak on

    the fruit immature fruit shown a green below while matured fruit shows yellow colour

    below the skin.

    Fruits ripe within 4-5 days. The unripe fruits can be stored at 500-520F for

    five weeks while ripe fruits can be stored at 320-350F.

    Yield up to 10 years- 750 fruits/ha.

    Yield 15 years - 1000 1500 fruits/ha.

    After 15 years yield - 2000-2500 fruits or 18-20 tons/ha.

    Highly susceptible to water logging and very densative to stagnation. It

    however tolerates considerable drought. The plant can tolerate extremes but the

    yield goes down as shadding of flowers occurs above 39 0C. Fair distribution or

    rains with mild summer helps in increasing the set. Ramphal cannot withstand

    severe summers or cold as that of sustard apple.

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    Fruit carbohydrates table:

    Fruit Carbohydrates Calories per piece

    Apple 10.5 grams 44

    Apple cooking 9 grams 35

    Apricot 6.7 grams 30

    Avocado 2 grams 150

    Banana 26 grams 107

    Blackberries each 0.2 grams 1

    Blackcurrant each 0.25 grams 1.1

    Cherry each 0.6 grams 2.4

    Clementine 7.5 grams 30

    Currants 1.4 grams 5

    Damson 7.2 grams 28

    Dates 3.3 grams 12.5

    Gooseberries 0.65 grams 2.6

    Grapes each 0.6 grams 2.4

    Grapefruit whole 23 grams 100

    Guava 4.4 grams 24

    Kiwi 8 grams 34

    Lemon 3.4 grams 20

    Lychees 0.7 grams 3

    Mango 9.5 grams 40

    Melon 26 grams 110

    Nectarines 9 grams 42

    Olives trace 6.8

    Orange 8.5 grams 35

    Passion Fruit 3 grams 30

    Paw Paw 6 grams 28

    Peach 7 grams 35

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    Pear 12 grams 45

    Pineapple 12 grams 50

    Plum 6 grams 25

    Prunes 2.2 grams 9

    Raisins 1.4 grams 5

    Raspberries each 0.2 grams 1.1

    Rhubarb 0.8 grams 8

    Satsumas 8.5 grams 35

    Strawberries (1 average) 0.6 grams 2.7

    Sultanas 1.4 grams 5

    Tangerine 6 grams 26

    Values for carbohydrates in fruit may vary between different sized pieces!

    Fruit Production and Acreage in Maharashtra

    Sr.

    No.

    Fruit Area Production

    1 Grapes 10,000 79,000

    2 Banana 53,800 14,18,7003 Mango 35,400 1,45,1404 Sweet orange 5,700 20,5205 Mandarin orange 33,600 1,51,2006 Kagzi lime 13,200 29,0407 Other citrus fruits 800 1,6008 Pomegranate 7,700 40,0409 Guava 8,500 39,95010 Custard apple 2,800 6,72011 Fig 200 16012 Jackfruit 300 326

    13 Papaya 1,500 11,25014 Sapota 3,900 10,92015 Cashew nut 19,000 5,89016 Others 23,700 18,480

    Total 2,20,100 19,78,936

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    Physical Properties of Ethanol

    Constants Absolute 95% (by

    vol)

    Boiling point,0

    C 78.3 78.0Electrical conductivity at 250C, Ohm-1/cm 1.35 x 10-9 -Explosive limits in air, vol % 4.3-19.0 -Flash point ( ASTM Tag Open Cup ), 0C 21 22Freezing point, 0C 114.1 -Heat of combustion of liquid, Kcal/mole 328 -Heat of fusion, cal/g 25.0 -Heat of vaporization at bp and 1 atm, cal/g 204.3 -Ignition temp.(apparent) in air, 0C 371-427 -Refractive index, n2D0 1.3614 1.3651Specific gravity at 20/20 0C 0.7905 0.8038

    Specific tension at 200C, dynes/cm 0.579 0.618Surface tension at 200C, dynes/cm 22.3 22.8Vapour pressure at 200C, mm Hg 44 43Viscosity at 20 0C, cps 1.22 1.41

    Chemical Properties : The chemical properties of ethanol are typical of n-

    saturated monohydric alcohols, especially in reactions which are concerned with the

    hydroxyl group. The ethyl group, however, does undergo several unique reactions,

    (as was previously noted for the methyl group of methanol).

    Alkylation. Ethanol is an important alkylating agent, especially with ammonia

    and the amines. This particular unit process is known ammonolysis and aminolysis,

    and the reaction with ammonia is shown below :

    CH3 CH2OH + NH3 CH3 CH2NH2 + H2O ethyl amine

    Sulfuric acid is known to dehydrate ethanol to ether in the manufacturing

    process which is based on hydration. Hydrochloric acid and alumina get are also

    commonly used as dehydratic catalysts.

    The aromatic nucleus may be alkylated with ethanol in the presence of a

    Friedel-Crafts catalyst :

    CH2 CH3+ H2O

    + CH3 CH2OH

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    ethyl benzene

    Concentrated sulfuric acid may from ethyl hydrogen sulfate if added slowly to

    ethanol :

    CH3 CH2OH + H2SO4 CH3 CH2 H2SO4 + H2O

    Slow distillation at reduced pressure will then form diethyl sulfate, an

    ethylating agent :

    2CH3 CH2 H2SO4 (CH3 CH2 )2SO4 + H2SO4

    Sulfur trioxide adds to ethanol and forms carbyl sulfate :

    CH3 CH2OH + 2SO3 CH2 CH2 O| | |

    SO2 O SO2 Carbyl sulfate

    Complex Formation. Ethanol behaves like water of crystallization and forms

    complexes with various inorganic compounds. The alcohol combines with calcium,

    magnesium, and platinum chlorides to form crystalline products.

    Dehydration. This reaction may proceed in two directions with ethanol. The

    intramolecular route to ethylene is favored when high temperatures and large

    catalyst ratios are employee :

    CH3 CH2OH CH2 = CH2 + H2O

    Intermolecular dehydration forms diethyl ether :

    2CH3 CH2OH CH3 CH2 O CH2 CH3 + H2O

    Ester Formation. Both inorganic and organic acids will form esters with

    ethanol :

    CH3 CH2OH + HNO3 CH3 CH2 NO3 + H2O ethyl nitrate

    Organic acids form organic esters and water :

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    CH3 CH2OH + RCOOH RCOOCH2 CH3 + H2O ester

    Since esterification is an equilibrium reaction, completion is favored by alarge excess of alcohol, by a large excess of acid, or by removal of water, Ethanol is

    quite low in cost; therefore, it is ordinarily the compound used in excess. Acid

    derivatives (such as acid chlorides, acid anhydrides, and simple alkyl esters of

    acids) will also form esters.

    Ethanol condenses with the carbonyl group of aldehydes and ketones at

    about 1000C to form acetals :

    2CH3 CH2OH + RCHO RCH(OCH2 CH3)2+ H2O

    The process of ester interchange is used to prepare ethyl esters from natural

    fats and oils :

    CH2OOCR CH2OH| |

    2CH3 CH2OH + CH2OOCR CH2OH + 3 RCOOCH2CH3| | ethyl esters

    CH2OOCR CH2OHglycerol

    Ethers. Ethyl ether formation is the result of an intermolecular catalytic

    dehydration of ethanol at low temperature :

    2CH3 CH2OH CH3 CH2OCH2 CH3 + H2O

    Vinyl ethyl ether or diethyl acetal are formed by the addition of ethanol to

    acetylene, the final product being dependent on whether an alkaline or acid catalyst

    is used :

    NaOC2H5

    CH3 CH2OH + CH CH CH3 CH2OCH2= CH2 Vinyl ethyl ether

    acid

    CH3 CH2OH + CH3 CH2OCH CH2 CH3 CH(OCH2CH3)2 catalyst diethyl acetal

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    Haloform Reaction, Ethanol may be oxidized by hypohalites to acetaldehyde

    and will then undergo the "haloform" reaction :

    CH3 CH2OH + NaOCl CH3 CHO + NaCl + H2O

    CH3 CHO + 3NaOCl CCl3 CHO + 3NaOH

    CCl3 CHO + NaOH CHCl3 + HCOONa

    Halogenation. Ethanol may undergo a typical reaction in which hydrogen

    halides, phosphorous halides, and similar reagents replace the hydroxyl group by

    halogen :

    3CH3 CH2OH + PCl 3CH3 CH2Cl + P(OH)3

    Oxidation. Conversion of ethanol to acetaldehyde can be accomplished byoxidation or dehydration. Air oxidation is carried out in the presence of copper and

    silver wire catalysts:

    Cu, Ag

    CH3 CH2OH + (O) CH3 CHO + H2O

    Dehydrogenation of ethanol is catalyzed by chromium-activated copper :

    Cu

    CH3 CH2OH CH3 CHO + H2

    Further oxidation of acetaldehyde leads to acetic acid :

    Cu

    CH3 CHO+ (O) CH3 COOH

    Direct chemical oxidation of ethanol to acetic acid in one step is not carried

    out commercially because of appreciable decomposition to carbon dioxide, carbon

    monoxide, methane and other low molecular weight compounds. However, one

    step oxidation to acetic acid is achieved industrially by fermentation.

    Reaction with Metals. Sodium, potassium and calcium may replace the

    hydroxyl hydrogen in ethanol to form a metal alkoxide (alcoholate):

    Cu, Ag

    2CH3 CH2OH + 2N 2CH3 CH2 ONa + H2 Sodium ethoxide

    Sodium and aluminum ethoxide are valuable agents in the field of organic

    synthesis.

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    Thermal Decomposition. Hearing ethanol above 800 C forms ethylene,

    acetaldehyde, water, and hydrogen. The use of a finely divided catalyst (such as

    alumina or metals) will cause decomposition at lower temperatures.

    FERMENTATION

    Fermenting fruits and vegetables can bring many benefits to people in

    developing countries. Fermented foods play an important role in providing food

    security, enhancing livelihoods and improving the nutrition and social well being of

    millions of people around the world, particularly the marginalised and vulnerable.

    Improving food security

    Eight hundred million people do not have enough food to eat. If we include those

    not free from hunger the figure rises to 1.2 billion people. This is one fifth of the

    World's population. A further two billion people are deficient in one or more micro-

    nutrients (Anon, 1996). In the seventies, food security was viewed mainly in terms

    of food supply at the global and national levels. Since then there has been a major

    shift in understanding of food security with more emphasis on access to food rather

    than purely on production. The Food and Agriculture Organisation of the United

    Nations (FAO), amongst other influential organisations, has recognised that the

    problem of food security cannot be tackled in isolation. Moreover that it is an

    integral component of other development issues. FAO highlights the fact that the

    world food insecurity problem is a result of undemocratic and inequitable distribution

    of and access to resources rather than a problem of global food production (Anon,

    1995), (Anon, 1996).

    Fermentation technologies play an important role in ensuring the food security of

    millions of people around the world, particularly marginalised and vulnerable

    groups. This is achieved through improved food preservation, increasing the range

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    of raw materials that can be used to produce edible food products and removing

    anti- nutritional factors to make food safe to eat.

    Food preservation

    Fermentation is a cheap and energy efficient means of preserving perishable raw

    materials. When harvested, fruit and vegetables, undergo rapid deterioration,

    especially in the humid tropics where the prevailing environmental conditions

    accelerate the process of decomposition. There are several options for preserving

    fresh fruit and vegetables including drying, freezing, canning and pickling. However

    many of these are inappropriate for use on the small-scale in developing countries.

    For instance the canning of vegetables at the small-scale has serious food safetyimplications and contamination with botulism is a possibility. Freezing of fruits and

    vegetables is not economically viable at the small-scale. Fermentation requires very

    little sophisticated equipment, either to carry out the fermentation or for subsequent

    storage of the fermented product. It is a technique that has been employed for

    generations to preserve food for consumption at a later date and to improve food

    security. There are examples from around the world of the role fermented foods

    have played in preserving food to enhance food security.

    Increasing income and employment

    The production of fermented fruit and vegetable products provides income and

    employment to millions of people around the world.

    Food processing is probably the most important source of income and employment

    in Africa, Asia and Latin America. The Food and Agriculture Organisation of the

    United Nations has stated that value added through marketing and processing rawproducts can be much greater than the value of primary production (Anon, 1995).

    For instance in sub-Saharan Africa more than 60% of the workforce is employed in

    the small scale food processing sector, and between one third and two thirds of

    value added manufacturing is based on agricultural raw materials (World Bank,

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    1989), (Conroy et al, 1995). This is particularly important as agriculture and the

    formal sector are unable to absorb the growing labour force in many countries.

    Fermented foods are popular throughout the world and the production of fermentedfood products is important in many countries in providing income and employment.

    In Africa, fermented cassava products (like Gariand Fufu) are a major component

    of the diet of more than 800 million people and in some parts of Africa it constitutes

    over 50% of the diet (Oyewole, 1992). In Asia the preparation of fermented foods is

    a widespread tradition. Kimchi (a fermented cabbage product) is the major food

    product of Korea. Soy sauce (a fermented legume product) is economically

    important from Indonesia to Japan. Over a billion litres are produced each year in

    Japan alone. Over 2000 million litres are produced each year in Korea and over 150

    million litres in Taiwan. Miso (a fermented legume product) is also very important in

    Asia with over 560,000 tons produced a year in Japan alone (Anon, 1982). In Latin

    America, fermented cereal products, alcoholic drinks and fermented milk products

    are three of the most important sectors of the economy.

    Improving nutrition

    The optimum health and nutrition of individuals is dependent upon a regular supply

    of food and a balanced diet. When diets are sub-optimal, the individual's capacity

    for work and achievements are greatly reduced. The most vulnerable groups are

    women, children and weaning infants. Availability of food, dietary restrictions and

    taboos, misconceptions, limited time available for feeding or eating compound to

    create a group of individuals who are nutritionally disadvantaged. Approximately

    30% of women consume less than their daily requirements of energy and at least

    40% of women world-wide suffer from iron-deficiency anaemia. Fermentation can

    enhance the nutritional value of a food product though increased vitamin levels and

    improved digestibility.

    Vitamins

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    Fermentation processes can result in increased levels of vitamins in the final

    product. Saccharomyces cerevisiae is able to concentrate large quantities of

    thiamin, nicotinic acid and biotin and thus form enriched products.

    Sorghum beer in Southern Africa contains relatively high levels of riboflavin

    and nicotinic acid, which are important for people consuming a high maize

    diet. Pellagra (a vitamin deficiency disease associated with high maize diets)

    is unusual in communities in which sorghum beer is consumed. Even

    children benefit from consuming the dregs which contain relatively little

    alcohol but are rich in vitamins.

    Palm wine in West Africa is high in vitamin B12, which is very important for

    people with low meat intake, and who subsist primarily on a vegetarian diet.

    Pulque (a fermented plant sap) is an important source of vitamins for the

    economically deprived in Mexico. The fermentation process involved in

    Pulque production increases its vitamin content. For instance the vitamin

    content (milligrams of vitamins per 100g of product) of pulque increases from

    5 to 29 for thiamine, 54 to 515 for niacin and 18 to 33 for riboflavin

    (Steinkraus, 1992) during fermentation.

    Idli (a lactic acid bacteria fermented product consumed in India) is high in

    thiamine and riboflavin.

    Digestibility

    Micro-organisms contain certain enzymes, such as cellulases, which are incapable

    of being synthesised by humans. Microbial cellulases hydrolyse cellulose into

    sugars which are then readily digestible by humans. Similarly pectinases soften the

    texture of foods and liberates sugars for digestion. Fermented foods are often moreeasily digestible than unfermented foods (Kovac, 1997), (Parades-Lopez, 1992).

    Lactic acid fermented weaning foods are traditionally produced in developing

    countries, both to improve the safety of the food and to improve its digestibility.

    Starchy porridges are commonly fed to weaning infants in developing countries. The

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    consistency of these gruels, combined with the small capacity of the infants

    stomach, means that it is physically impossible for the child to consume adequate

    energy to meet its high demands. By acidifying the porridge through lactic acid

    fermentation, starch is hydrolysed into shorter chains of glucose and dextrose,

    which reduce the viscosity of the porridge and increase its energy density. Thus the

    child is more able to meet its energy requirements.

    Medicinal benefits

    There are many traditional beliefs about the medicinal properties of fermented food

    products. The Fur ethnic group in Sudan strongly believe that the consumption of

    fermented foods protects them from disease (Dirar, 1992). Koumiss (a fermented

    milk product in Russia) has been used to treat tuberculosis. Pulque (a fermented

    fruit sap) is felt to have medicinal properties in Mexico.

    There is a sound scientific basis to these assertions:

    The lowering of the pH inhibits the growth of food spoiling or poisoning

    bacteria and destroys certain pathogens (Hammes, and Tichaczek, 1994).

    Certain lactic acid bacteria (e.g. Lactobacillusacidophilus) and moulds have

    been found to produce antibiotics and bacteriocins (Wood and Hodge, 1985)

    (Matususaki et al, 1997) (Adams and Nicolaides, 1997), (Gourama and

    Bullerman, 1995), (Nout, 1995)..

    The beneficial health effects of lactic acid bacteria on the intestinal flora are

    well documented (Ottogalli and Galli, 1997), (Motarjemi et al, 1996).

    Substances in fermented foods have been found to have a protective effect

    against the development of cancer (Frohlich et al, 1997).

    Fermentation is a traditional method of reducing the microbial contamination of

    porridges in Kenya (Watson, Ngesa, Onyang, Alnwick and Tomkins, 1996) A study

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    in Tanzania has shown that children fed with fermented gruels had a 33% lower

    incidence of diarrhoea than those fed unfermented gruels, owing to the inhibition of

    pathogenic bacteria by lactic acid forming bacteria (Svanberg, 1992).

    Improving cultural and social well being

    Fermentation can improve the flavour and appearance of food. One important area

    is the creation of meat-like flavour. Over the years, Sudanese women have

    developed products to replace meat in their diets. These include "kawal", fermented

    wild legume leaves, "sigda" (fermented sesame press-cake) and "furundu"

    (fermented red sorrel seeds). The strong flavours of fermented food products can

    enhance a dull diet. Fermented vegetables such as pickles, gundrukand sauerkraut

    are used as condiments to enhance the overall flavour of the meal. A small amount

    of pickle can make a bland starchy diet (like dahl and rice in Asia) much more

    appealing (Battcock, 1992).

    The diversity of fermented foods

    Numerous fermented foods are consumed around the world. Each nation has its

    own types of fermented food, representing the staple diet and the raw ingredientsavailable in that particular place. Although the products are well know to the

    individual, they may not be associated with fermentation. Indeed, it is likely that the

    methods of producing many of the worlds fermented foods are unknown and came

    about by chance. Some of the more obvious fermented fruit and vegetable products

    are the alcoholic beverages - beers and wines. However, several more fermented

    fruit and vegetable products arise from lactic acid fermentation and are extremely

    important in meeting the nutritional requirements of a large proportion of the worlds

    population. Table 2.1 contains examples of fermented fruit and vegetable products

    from around the world.

    Organisms responsible for food fermentations

    The most common groups of micro-organisms involved in food fermentations are:

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    Bacteria

    Yeasts

    Moulds

    1 Bacteria

    Several bacterial families are present in foods, the majority of which are concerned

    with food spoilage. As a result, the important role of bacteria in the fermentation of

    foods is often overlooked. The most important bacteria in desirable food

    fermentations are the lactobacillaceae which have the ability to produce lactic acid

    from carbohydrates. Other important bacteria, especially in the fermentation of fruits

    and vegetables, are the acetic acid producing acetobacterspecies.

    2 Yeasts

    Yeasts and yeast-like fungi are widely distributed in nature. They are present in

    orchards and vineyards, in the air, the soil and in the intestinal tract of animals. Like

    bacteria and moulds, yeasts can have beneficial and non-beneficial effects in foods.

    The most beneficial yeasts in terms of desirable food fermentation are from the

    Saccharomyces family, especially S. cerevisiae. Yeasts are unicellular organisms

    that reproduce asexually by budding. In general, yeasts are larger than most

    bacteria. Yeasts play an important role in the food industry as they produce

    enzymes that favour desirable chemical reactions such as the leavening of bread

    and the production of alcohol and invert sugar.

    Table 1 : Fermented foods from around the world.

    Name and region Type of product

    Indian sub-continent

    Acar, Achar, Tandal achar, Garam nimboo achar Pickled fruit and vegetables

    Gundruk Fermented dried vegetable

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    Lemon pickle, Lime pickle, Mango pickle

    South East Asia

    Asinan, Burong mangga, Dalok, Jeruk, Kiam-chai,

    Kiam-cheyi, Kong-chai, Naw-mai-dong, Pak-siam-

    dong, Paw-tsay, Phak-dong, Phonlami-dong,

    Sajur asin, Sambal tempo-jak, Santol, Si-sek-chai,

    Sunki, Tang-chai, Tempoyak, Vanilla,

    Pickled fruit and vegetables

    Bai-ming, Leppet-so, Miang Fermented tea leaves

    Nata de coco, Nata de pina Fermented fruit juice

    East Asia

    Bossam-kimchi, Chonggak-kimchi, Dan moogi,

    Dongchimi, Kachdoo kigactuki, Kakduggi, Kimchi,

    Mootsanji, Muchung-kimchi, Oigee, Oiji, Oiso

    baegi, Tongbaechu-kimchi, Tongkimchi, Totkal

    kimchi,

    Fermented in brine

    Cha-tsai, Hiroshimana, Jangagee, Nara senkei,Narazuke, Nozawana, Nukamiso-zuke, Omizuke,

    Pow tsai, Red in snow, Seokbakji, Shiozuke,

    Szechwan cabbage, Tai-tan tsoi, Takana, Takuan,

    Tsa Tzai, Tsu, Umeboshi, Wasabi-zuke, Yen tsai

    Pickled fruit and vegetables

    Hot pepper sauce

    Africa

    Fruit vinegar Vinegar

    Hot pepper sauce

    Lamoun makbouss, Mauoloh, Msir, Mslalla, Olive Pickled fruit and vegetables

    Oilseeds, Ogili, Ogiri, Hibiscus seed Fermented fruit and vegetable

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    seeds

    Wines Fermented fruits

    Americas

    Cucumber pickles, Dill pickles, Olives, Sauerkraut, Pickled fruit and vegetables

    Lupin seed, Oilseeds, Pickled oilseed

    Vanilla, Wines Fermented fruit and vegetable

    Middle East

    Kushuk Fermented fruit and

    vegetables

    Lamoun makbouss, Mekhalel, Olives, Torshi,

    Tursu

    Pickled fruit and vegetables

    Wines Fermented fruits

    Europe and World

    Mushrooms, Yeast Moulds

    Olives, Sauerkohl, Sauerruben Pickled fruit and vegetables

    Grape vinegar, Wine vinegar Vinegar

    Wines, Citron Fermented fruits

    (Taken from G Campbell-Platt (1987))

    Moulds

    Moulds are also important organisms in the food industry, both as spoilers and

    preservers of foods. Certain moulds produce undesirable toxins and contribute to

    the spoilage of foods. TheAspergillus species are often responsible for undesirable

    changes in foods. These moulds are frequently found in foods and can tolerate high

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    concentrations of salt and sugar. However, others impart characteristic flavours to

    foods and others produce enzymes, such as amylase for bread making. Moulds

    from the genus Penicillium are associated with the ripening and flavour of cheeses.

    Moulds are aerobic and therefore require oxygen for growth. They also have the

    greatest array of enzymes, and can colonise and grow on most types of food.

    Moulds do not play a significant role in the desirable fermentation of fruit and

    vegetable products.

    When micro-organisms metabolise and grow they release by-products. In food

    fermentations the by-products play a beneficial role in preserving and changing the

    texture and flavour of the food substrate. For example, acetic acid is the by-product

    of the fermentations of some fruits. This acid not only affects the flavour of the final

    product, but more importantly has a preservative effect on the food. For food

    fermentations, micro-organisms are often classified according to these by-products.

    The fermentation of milk to yoghurt involves a specific group of bacteria called the

    lactic acid bacteria (Lactobacillus species). This is a general name attributed to

    those bacteria which produce lactic acid as they grow. Acidic foods are less

    susceptible to spoilage than neutral or alkaline foods and hence the acid helps to

    preserve the product. Fermentations also result in a change in texture. In the case

    of milk, the acid causes the precipitation of milk protein to a solid curd.

    Enzymes

    The changes that occur during fermentation of foods are the result of enzymic

    activity. Enzymes are complex proteins produced by living cells to carry out specific

    biochemical reactions. They are known as catalysts since their role is to initiate and

    control reactions, rather than being used in a reaction. Because they areproteinaceous in nature, they are sensitive to fluctuations in temperature, pH,

    moisture content, ionic strength and concentrations of substrate and inhibitors. Each

    enzyme has requirements at which it will operate most efficiently. Extremes of

    temperature and pH will denature the protein and destroy enzyme activity. Because

    they are so sensitive, enzymic reactions can easily be controlled by slight

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    adjustments to temperature, pH or other reaction conditions. In the food industry,

    enzymes have several roles - the liquefaction and saccharification of starch, the

    conversion of sugars and the modification of proteins. Microbial enzymes play a role

    in the fermentation of fruits and vegetables.

    Nearly all food fermentations are the result of more than one micro-organism, either

    working together or in a sequence. For example, vinegar production is a joint effort

    between yeast and acetic acid forming bacteria. The yeast convert sugars to

    alcohol, which is the substrate required by the acetobacter to produce acetic acid.

    Bacteria from different species and the various micro-organisms - yeast and moulds

    -all have their own preferences for growing conditions, which are set within narrow

    limits. There are very few pure culture fermentations. An organism that initiates

    fermentation will grow there until its by-products inhibit further growth and activity.

    During this initial growth period, other organisms develop which are ready to take

    over when the conditions become intolerable for the former ones.

    In general, growth will be initiated by bacteria, followed by yeasts and then moulds.

    There are definite reasons for this type of sequence. The smaller micro-organisms

    are the ones that multiply and take up nutrients from the surrounding area mostrapidly. Bacteria are the smallest of micro-organisms, followed by yeasts and

    moulds. The smaller bacteria, such as Leuconostocand Streptococcusgrow and

    ferment more rapidly than their close relations and are therefore often the first

    species to colonise a substrate (Mountney and Gould, 1988).

    Table 2 : Micro-organisms commonly found in fermenting fruit and vegetables

    Organism Type Optimum

    conditions

    Reactions

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    Acetobacter genus

    A. aceti

    A. pasteurianus

    A. peroxydans

    Aerobic

    rods

    aw > =0.9 Oxidise organic compounds

    (alcohol) to organic acids

    (acetic acid). Important in

    vinegar production.

    Streptococcaceae

    Family

    Gram

    positive

    cocci

    Acid

    tolerant

    aw > =0.9

    Streptococcus genus

    S. faecalis

    S. bovis

    S. thermophilus

    Homofermentative. Most

    common in dairy

    fermentations, but S. Faecalis

    is common in vegetable

    products. Tolerate salt and

    can grow in high pH media.

    Leuconostoc genus

    L. mesenteroides

    L. dextranicum

    L.

    paramesenteroides

    L. oenos

    Gram

    positive

    cocci

    Heterofermentative. Produce

    lactic acid, plus acetic acid,

    ethanol and carbon dioxide

    from glucose. Small bacteria,

    therefore have an important

    role in initiating fermentations.

    L. oenos is often present in

    wine. It can utilise malic acid

    and other organic acids.

    Pediococcus genus

    P. cerevisiae

    P. acidilactici

    P. pentosaceus

    Saprophytic organisms found

    in fermenting vegetables,

    mashes, beer and wort.

    Produce inactive lactic acid.

    Lactobacillaceae Gram Acid Metabolise sugars to lactic

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    Family positive

    rods. Non-

    motile

    tolerant

    aw > =0.9

    acid, acetic acid, ethyl alcohol

    and carbon dioxide.

    Lactobacillus genus The genus is split into two

    types homo- and hetero-

    fermenters. Saprophytic

    organisms. Produce greater

    amounts of acid than the cocci

    Homofermentative

    Lactobacillus spp.L. delbrueckii

    L. leichmannii

    L. plantarum

    L. lactis

    L. acidophilus

    Produce only lactic acid. L.

    plantarum important in fruitand vegetable fermentation.

    Tolerates high salt

    concentration.

    Heterofermentative

    Spp.L. brevis

    L. fermentum

    L. buchneri

    Produce lactic acid (50%) plus

    acetic acid (25%), ethylalcohol and carbon dioxide

    (25%). L. brevis is the most

    common. Widely distributed in

    plants and animals. Partially

    reduces fructose to mannitol.

    Yeasts Tolerate

    acid, 40%sugar

    aw > =0.85

    Saccharomyces

    Cerevisiae

    Many

    aerobic,

    pH 4-4.5

    20-30 C

    S. cerevisiae can shift its

    metabolism from a

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    S. pombe some

    anaerobes

    fermentative to an oxidative

    pathway, depending on

    oxygen availability. Most

    yeasts produce alcohol and

    carbon dioxide from sugars.

    Debaromyces

    Zygosaccharomyces

    rouxii

    Candida species

    Geotrichum

    candidum

    Tolerant of high salt

    concentrations

    Tolerates high salt

    concentration and low aw

    Desirable fermentation

    It is essential with any fermentation to ensure that only the desired bacteria, yeasts

    or moulds start to multiply and grow on the substrate. This has the effect of

    suppressing other micro-organisms which may be either pathogenic and cause food

    poisoning or will generally spoil the fermentation process, resulting in an end-

    product which is neither expected or desired. An everyday example used to

    illustrate this point is the differences in spoilage between pasteurised and

    unpasteurised milk. Unpasteurised milk will spoil naturally to produce a sour tasting

    product which can be used in baking to improve the texture of certain breads.

    Pasteurised milk, however, spoils (non-desirable fermentation) to produce an

    unpleasant product which has to be disposed of. The reason for this difference is

    that pasteurisation (despite being a very important process to destroy pathogenic

    micro-organisms) changes the micro-organism environment and if pasteurised milk

    is kept unrefrigerated for some time, undesirable micro-organisms start to grow and

    multiply before the desirable ones. In the case of unpasteurised milk, the non-

    pathogenic lactic acid bacteria start to grow and multiply at a greater rate that any

    pathogenic bacteria. Not only do the larger numbers of lactic acid bacteria compete

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    more successfully for the available nutrients, but as they grow they produce lactic

    acid which increases the acidity of the substrate and further suppresses the bacteria

    which cannot tolerate an acid environment.

    Most food spoilage organisms cannot survive in either alcoholic or acidic

    environments. Therefore, the production of both these end products can prevent a

    food from spoilage and extend the shelf life. Alcoholic and acidic fermentations

    generally offer cost effective methods of preserving food for people in developing

    countries, where more sophisticated means of preservation are unaffordable and

    therefore not an option.

    The principles of microbial action are identical both in the use of micro-organisms in

    food preservation, such as through desirable fermentations, and also as agents of

    destruction via food spoilage. The type of organisms present and the environmental

    conditions will determine the nature of the reaction and the ultimate products. By

    manipulating the external reaction conditions, microbial reactions can be controlled

    to produce desirable results. There are several means of altering the reaction

    environment to encourage the growth of desirable organisms. These are discussed

    below.

    Manipulation of microbial growth and activity

    There are six major factors that influence the growth and activity of micro-organisms

    in foods. These are moisture, oxygen concentration, temperature, nutrients, pH and

    inhibitors (Mountney and Gould, 1988). The food supply available to the micro-

    organisms depends on the composition of the food on which they grow. All micro-

    organisms differ in their ability to metabolise proteins, carbohydrates and fats.

    Obviously, by manipulating any of these six factors, the activity of micro-organisms

    within foods can be controlled.

    Moisture

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    Water is essential for the growth and metabolism of all cells. If it is reduced or

    removed, cellular activity is decreased. For example, the removal of water from cells

    by drying or the change in state of water (from liquid to solid) affected by freezing,

    reduces the availability of water to cells (including microbial cells) for metabolic

    activity. The form in which water exists within the food is important as far as

    microbial activity is concerned. There are two types of water - free and bound.

    Bound water is present within the tissue and is vital to all the physiological

    processes within the cell. Free water exists in and around the tissues and can be

    removed from cells without seriously interfering with the vital processes. Free water

    is essential for the survival and activity of micro-organisms. Therefore, by removing

    free water, the level of microbial activity can be controlled. The amount of wateravailable for micro-organisms is referred to as the water activity (aw). Pure water

    has a water activity of 1.0. Bacteria require more water than yeasts, which require

    more water than moulds to carry out their metabolic activities. Almost all microbial

    activity is inhibited below aw of 0.6. Most fungi are inhibited below aw of 0.7, most

    yeasts are inhibited below aw of 0.8 and most bacteria below aw 0.9. Naturally, there

    are exceptions to these guidelines and several species of micro-organism can exist

    outside the stated range. See table for further information on water activity and

    microbial action. The water activity of foods can be changed by altering the amount

    of free water available. There are several ways to achieve this drying to remove

    water; freezing to change the state of water from liquid to solid; increasing or

    decreasing the concentration of solutes by adding salt or sugar or other hydrophylic

    compounds (salt and sugar are the two common additives used for food

    preservation). Addition of salt or sugar to a food will bind free water and so

    decrease the aw. Alternatively, decreasing the concentration will increase the

    amount of free water and in turn the aw. Manipulation of the aw in this manner can be

    used to encourage the growth of favourable micro-organisms and discourage the

    growth of spoilage ones.

    Table 3: Water activity for microbial reactions

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    Aw Phenomenon Examples

    1.00 Highly perishable foods

    0.95 Pseudomonas, Bacillus,

    Clostridium perfringens and some

    yeasts inhibited

    Foods with 40% sucrose or 7%

    salt

    0.90 Lower limit for bacterial growth.

    Salmonella, Vibrio

    parahaemolyticus, Clostridium

    botulinum, Lactobacillus and some

    yeasts and fungi inhibited

    Foods with 55% sucrose, 12% salt.

    Intermediate-moisture foods (aw =

    0.90-0.55)

    0.85 Many yeasts inhibited Foods with 65% sucrose, 15% salt

    0.80 Lower limit for most enzyme

    activity and growth of most fungi.

    Staphylococcus aureus inhibited

    Fruit syrups

    0.75 Lower limit for halophilic bacteria Fruit jams

    0.70 Lower limit for growth of mostxerophilic fungi

    0.65 Maximum velocity of Maillard

    reactions

    0.60 Lower limt for growth of osmophilic

    or xerophilic yeasts and fungi

    Dried fruits (15-20% water)

    0.55 Deoxyribose nucleic acid (DNA)

    becomes disordered (lower limit

    for life to continue)

    0.50 Dried foods (aw=0-0.55)

    0.40 Maximum oxidation velocity

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    0.25 Maximum heat resistance of

    bacterial spores

    Taken from Fellows (1988).

    Oxidation-Reduction potential

    Oxygen is essential to carry out metabolic activities that support all forms of life.

    Free atmospheric oxygen is utilised by some groups of micro-organisms, while

    others are able to metabolise the oxygen which is bound to other compounds such

    as carbohydrates. This bound oxygen is in a reduced form.

    Micro-organisms can be broadly classified into two groups - aerobic and anaerobic.

    Aerobes grow in the presence of atmospheric oxygen while anaerobes grow in the

    absence of atmospheric oxygen. In the middle of these two extremes are the

    facultative anaerobes which can adapt to the prevailing conditions and grow in

    either the absence or presence of atmospheric oxygen. Microaerophilic organisms

    grow in the presence of reduced amounts of atmospheric oxygen. Thus, controlling

    the availability of free oxygen is one means of controlling microbial activity within a

    food. In aerobic fermentations, the amount of oxygen present is one of the limiting

    factors. It determines the type and amount of biological product obtained, the

    amount of substrate consumed and the energy released from the reaction.

    Moulds do not grow well in anaerobic conditions, therefore they are not important in

    terms of food spoilage or beneficial fermentation, in conditions of low oxygen

    availability.

    Temperature

    Temperature affects the growth and activity of all living cells. At high temperatures,

    organisms are destroyed, while at low temperatures, their rate of activity is

    decreased or suspended. Micro-organisms can be classified into three distinct

    categories according to their temperature preference (see table2.4).

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    Table 4 Classification of bacteria according to temperature requirements.

    Temperature required for growth 0C

    Type of

    bacteria

    Minimum optimum maximum General sources of

    bacteria

    Psychrophilic 0 to 5 15 to 20 30 Water and frozen foods

    Mesophilic 10 to 25 30 to 40 35 to 50 Pathogenic and non-

    pathogenic bacteria

    Thermophilic 25 to 45 50 to 55 70 to 90 Spore forming bacteria

    from soil and water

    (Taken from Mountney and Gould, (1988).

    Nutritional requirements

    The majority of organisms are dependent on nutrients for both energy and growth.

    Organisms vary in their specificity towards different substrates and usually only

    colonise foods which contain the substrates they require. Sources of energy varyfrom simple sugars to complex carbohydrates and proteins. The energy

    requirements of micro-organisms are very high. Limiting the amount of substrate

    available can check their growth.

    Hydrogen ion concentration (pH)

    The pH of a substrate is a measure of the hydrogen ion concentration. A food with a

    pH of 4.6 or less is termed a high acid or acid food and will not permit the growth of

    bacterial spores. Foods with a pH above 4.6. are termed low acid and will not inhibit

    the growth of bacterial spores. By acidifying foods and achieving a final pH of less

    than 4.6, most foods are resistant to bacterial spoilage.

    The optimum pH for most micro-organisms is near the neutral point (pH 7.0).

    Certain bacteria are acid tolerant and will survive at reduced pH levels. Notable

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    acid-tolerant bacteria include the Lactobacillus and Streptococcus species, which

    play a role in the fermentation of dairy and vegetable products. Moulds and yeasts

    are usually acid tolerant and are therefore associated with spoilage of acidic foods.

    Micro-organisms vary in their optimal pH requirements for growth. Most bacteria

    favour conditions with a near neutral pH (7). Yeasts can grow in a pH range of 4 to

    4.5 and moulds can grow from pH 2 to 8.5, but favour an acid pH. The varied pH

    requirements of different groups of micro-organisms is used to good effect in

    fermented foods where successions of micro-organisms take over from each other

    as the pH of the environment changes. For instance, some groups of micro-

    organisms ferment sugars so that the pH becomes too low for the survival of those

    microbes. The acidophilic micro-organisms then take over and continue the

    reaction. The affinity for different pH can also be used to good effect to occlude

    spoilage organisms.

    Inhibitors

    Many chemical compounds can inhibit the growth and activity of micro-organisms.

    They do so by preventing metabolism, denaturation of the protein or by causing

    physical damage to the cell. The production of substrates as part of the metabolic

    reaction also acts to inhibit microbial action.

    Controlled fermentation

    Controlled fermentations are used to produce a range of fermented foods, including

    sauerkraut, pickles, olives, vinegar, dairy and other products. Controlled

    fermentation is a form of food preservation since it generally results in a reduction of

    acidity of the food, thus preventing the growth of spoilage micro-organisms. The twomost common acids produced are lactic acid and acetic acid, although small

    amounts of other acids such as propionic, fumaric and malic acid are also formed

    during fermentation.

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    It is highly probable that the first controlled food fermentations came into existence

    through trial and error and a need to preserve foods for consumption later in the

    season. It is possible that the initial attempts at preservation involved the addition of

    salt or seawater. During the removal of the salt prior to consumption, the foods

    would pass through stages favourable to acid fermentation. Although the process

    worked, it is likely that the causative agents were unknown. Today, there are

    numerous examples of controlled fermentation for the preservation and processing

    of foods. However, only a few of these have been studied in any detail - these

    include sauerkraut, pickles, kimchi, beer, wine and vinegar production. Although the

    general principles and processes for many of the fermented fruit and vegetable

    products are the same -relying mainly on lactic acid and acetic acid formingbacteria, yeasts and moulds, the reactions have not been quantified for each

    product. The reactions are usually very complex and involve a series of micro-

    organisms, either working together or in succession to achieve the final product.

    What are yeasts?

    A yeast is a unicellular fungus which reproduces asexually by budding or division,

    especially the genus Saccharomyces which is important in food fermentations

    (Walker, 1988). Yeasts and yeast-like fungi are widely distributed in nature. They

    are present in orchards and vineyards, in the air, the soil and the intestinal tract of

    animals. Like bacteria and moulds, they can have beneficial and non-beneficial

    effects in foods. Most yeasts are larger than most bacteria. The most well known

    examples of yeast fermentation are in the production of alcoholic drinks and the

    leavening of bread. For their participation in these two processes, yeasts are ofmajor importance in the food industry.

    Some yeasts are chromogenic and produce a variety of pigments, including green,

    yellow and black. Others are capable of synthesising essential B group vitamins.

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    Although there is a large diversity of yeasts and yeast-like fungi, (about 500

    species), only a few are commonly associated with the production of fermented

    foods. They are all either ascomycetous yeasts or members of the genus Candida.

    Varieties of the Saccharomyces cervisiae genus are the most common yeasts in

    fermented foods and beverages based on fruit and vegetables. All strains of this

    genus ferment glucose and many ferment other plant derived carbohydrates such

    as sucrose, maltose and raffinose. In the tropics, Saccharomycespombe is the

    dominant yeast in the production of traditional fermented beverages, especially

    those derived from maize and millet (Adams and Moss, 1995).

    Conditions necessary for fermentation

    Most yeasts require an abundance of oxygen for growth, therefore by controlling the

    supply of oxygen, their growth can be checked. In addition to oxygen, they require a

    basic substrate such as sugar. Some yeasts can ferment sugars to alcohol and

    carbon dioxide in the absence of air but require oxygen for growth. They produce

    ethyl alcohol and carbon dioxide from simple sugars such as glucose and fructose.

    C6H12O6 2C2H5OH + 2CO2

    Glucose yeast ethyl alcohol carbon dioxide

    In conditions of excess oxygen (and in the presence of acetobacter) the alcohol can

    be oxidised to form acetic acid. This is undesirable if the end product is a fruit

    alcohol, but is a technique employed for the production of fruit vinegars (see later

    section on mixed fermentations).

    Yeasts are active in a very broad temperature range - from 0 to 50 0 C, with an

    optimum temperature range of 200 to 300 C.

    The optimum pH for most micro-organisms is near the neutral point (pH 7.0).

    Moulds and yeasts are usually acid tolerant and are therefore associated with the

    spoilage of acidic foods. Yeasts can grow in a pH range of 4 to 4.5 and moulds can

    grow from pH 2 to 8.5, but favour an acid pH (Mountney and Gould, 1988).

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    In terms of water requirements, yeasts are intermediate between bacteria and

    moulds. Bacteria have the highest demands for water, while moulds have the least

    need. Normal yeasts require a minimum water activity of 0.85 or a relative humidity

    of 88%.

    Yeasts are fairly tolerant of high concentrations of sugar and grow well in solutions

    containing 40% sugar. At concentrations higher than this, only a certain group of

    yeasts the osmophilic type can survive. There are only a few yeasts that can

    tolerate sugar concentrations of 65-70% and these grow very slowly in these

    conditions (Board, 1983). Some yeasts for example the Debaromyces - can

    tolerate high salt concentrations. Another group which can tolerate high salt

    concentrations and low water activity is Zygosaccharomyces rouxii, which is

    associated with fermentations in which salting is an integral part of the process.

    Production of fruit alcohol

    Alcohol and acids are two primary products of fermentation, both used to good

    effect in the preservation of foods. Several alcohol-fermented foods are preceded

    by an acid fermentation and in the presence of oxygen and acetobacter, alcohol can

    be fermented to produce acetic acid. Most food spoilage organisms cannot survive

    in either alcoholic or acidic environments. Therefore, the production of both these

    end products can prevent a food from undergoing spoilage and extend its shelf life.

    Primitive wines and beers have been produced, with the aid of yeasts, for

    thousands of years, although it was not until about four hundred years ago thatmicro-organisms associated with the fermentation were observed and identified. It

    was not until the 1850s that Louis Pasteur demonstrated unequivocally the

    involvement of yeasts in the production of wines and beers (Fleet, 1998). Since

    then, the knowledge of yeasts and the conditions necessary for fermentation of wine

    and beer has increased to the point where pure culture fermentations are now used

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    to ensure consistent product quality. Originally, alcoholic fermentations would have

    been spontaneous events that resulted from the activity of micro-organisms

    naturally present. These non-scientific methods are still used today for the home

    preparation of many of the worlds traditional beers and wines.

    Alcoholic drinks fall into two broad categories: wines and beers. Wines are made

    from the juice of fruits and beers from cereal grains. The principal carbohydrates in

    fruit juices are soluble sugars; the principal carbohydrate in grains is starch, an

    insoluble polysaccharide. The yeasts that bring about alcoholic fermentation can

    attack soluble sugars but do not produce starch-splitting enzymes. Wines can

    therefore be made by the direct fermentation of the raw material, while the

    production of beer requires the hydrolysis of starch to yield sugars fermentable byyeast, as a preliminary step (Stanier, Dourdoff and Adelberg, 1972).

    Raw fruit juice is usually a strongly acidic solution, containing from 10 to 25 percent

    soluble sugars. Its acidity and high sugar concentration make it an unfavourable

    medium for the growth of bacteria but highly suitable for yeasts and moulds. Raw

    fruit juice naturally contains many yeasts, moulds, and bacteria, derived from the

    surface of the fruit. Normally the yeast used in alcoholic fermentation is a strain of

    the species Saccharomyces cerevisiae (Adams, 1985).

    The fermentation may be allowed to proceed spontaneously, or can be "started" by

    inoculation with a must that has been previously successfully fermented by S.

    cerevisiae var. ellipsoideus. Many modern wineries eliminate the original microbial

    population of the must by pasteurisation or by treatment with sulphur dioxide. The

    must is then inoculated with a starter culture derived from a pure culture of a

    suitable strain of wine yeast. This procedure eliminates many of the uncertainties

    and difficulties of older methods. At the start of the fermentation, the must is aerated

    slightly to build up a large and vigorous yeast population; once fermentation sets in,

    the rapid production of carbon dioxide maintains anaerobic conditions, which

    prevent the growth of undesirable aerobic organisms, such as bacteria and moulds.

    The temperature of fermentation is usually from 25 to 30 oC, and the duration of the

    fermentation process may extend from a few days to two weeks. As soon as the

    desired degree of sugar disappearance and alcohol production has been attained,

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    the microbiological phase of wine making is over. Thereafter, the quality and

    stability of the wine depend very largely on preventing further microbial activity, both

    during the "aging" in wooden casks and after bottling (Stanieret al, 1972).

    At all stages during its manufacture, fruit juice alcohol is subject to spoilage by

    undesirable microorganisms. Pasteur, whose descriptions of the organisms

    responsible and recommendations for overcoming them are still valid today, first

    scientifically explored the problem of the "diseases" of wines. The most serious

    aerobic spoilage processes are brought about by film-forming yeasts and acetic

    acid bacteria, both of which grow at the expense of the alcohol, converting it to

    acetic acid or to carbon dioxide and water. The chief danger from these organisms

    arises when access of air is not carefully regulated during aging. Much more seriousare the diseases caused by fermentative bacteria, particularly rod-shaped lactic acid

    bacteria, which utilise any residual sugar and impart a mousy taste to the wine.

    Such wines are known as turned wines. Since oxygen is unnecessary for the growth

    of lactic acid bacteria, wine spoilage of this kind can occur even after bottling. These

    risks of spoilage can be minimised by pasteurisation after bottling.

    Fermentation pathways

    The initial steps are identical to those of respiration. For example, forcarbohydrate fermentation, the pathway begins with glycolysis. In EM glycolytic

    pathway, there are generated two pyruvate molecules, two reduced coenzyme

    NADH molecules, and two ATP molecules for each molecule of glucose. The

    remainder of the fermentation pathway is concerned with reoxidising the coenzyme.

    In fermentation, reoxidation of NADH to NAD+ depends on the reduction of

    pyruvate molecules formed during glycolysis. Different microorganisms have

    developed different pathways for utilising the pyruvate for reoxidising the reduced

    coenzyme with different terminal sequences of the various fermentation pathways

    resulting in the formation of various end products (Fig). The different fermentation

    pathways are named for the characteristic end products that are formed. The most

    common ones are as follows :

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    Batch Growth of Micro-Organism

    The batch growth of micro-organisms involves adding a small quantity of the

    micro-organisms or their spores (the seed culture or inoculum) to a quantity of

    nutrient material in a suitable vessel. In the case of an aerobic fermentation (i.e. a

    growth process requiring the presence of molecular oxygen) the contents of the

    vessel (or fermenter) are aerated and the growth of the micro-organism allowed to

    proceed. For convenience, the case where the feed material is present in aqueous

    solution is considered and, furthermore, it is assumed that in the feed there is

    contained a carbon and energy source which is the limiting substrate for the growth

    of the culture. Whilst for an aerobic culture aeration is of prime importance, the factthat air enters the vessel and leaves enriched in carbon dioxide will be ignored in

    this discussion and the analysis focused on the changes occurring in the liquid

    phase.

    C.O.E.& T.,Akola 40

    Fig. The ethanolicfermentation pathway

    Fig. The homolactic acid fermentation

    pathway End product is lactic acid (lactate)

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    After inoculation, assuming no lag phase, the resultant growth can be

    analysed by considering the unsteady-state material balances for the substrate and

    biomass. The general form of this balance for a fermenter is :

    + = Accumulation

    Since a batch process is being considered, the flow in and out of the fermenter are

    both zero and the expression reduces to:

    = Accumulation

    So, for the case of the biomass:

    VdT

    dxVXVRx == (1)

    where is the specific growth rate, V is the volume of the vessel and X is the

    instantaneous concentration of the biomass. IfY is the overall yield coefficient for

    the formation of biomass and the limiting substrate concentration is 5, then the

    equivalent expression for substrate is:

    VdTdSVRS = (2)

    where Rs is the rate of conversion of substrate per unit volume of the reactor.

    Equation 5.116 makes no assumptions regarding the uniformity of the yield

    coefficient Yx/s, but if that can be taken to be constant then equation may be used to

    relate equations (1) and (2). This condition is met when is large in comparison

    with m so that, dispensing with the subscript, the differential form of equation can be

    written:

    dt

    dX

    dt

    dSY =

    (3)

    which gives:

    YRs = - X (4)

    Equation 2 thus becomes:

    C.O.E.& T.,Akola 41

    Flow of

    material inFormation by

    biochemical

    Flow of

    material out

    Formation by

    biochemical

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    Manufacturing of Ethyl Alcohol from Fruit Waste

    dt

    dSXY

    = 1

    (5)

    The yield coefficient may also be expressed in its integral form as:

    SS

    XXY

    =0

    0

    (6)

    which can be re-arranged:

    Y

    XXSS 00

    = (6)

    If the growth follows the Monod kinetic model, then equation may be substituted into

    equation 1 to give:

    SK

    SX

    dt

    dX

    s

    m

    +=

    (7)

    The condition of the fermentation after any time / would then be given by:

    =+ tX

    X m

    s dtX

    dX

    S

    SK

    00

    (8)

    However, S is a. function ofX and substitution using equation 6 must be made

    before carrying out the integration. The result is:

    ++

    +

    +++

    )XXYS(

    YSln

    )XYS(

    YK

    X

    Xln

    )XYS(

    XYSYK

    m

    S

    m

    S

    00

    0

    00000

    00

    (9)

    A similar expression can be obtained for the substrate concentration:

    tS

    Sln

    )YSX(

    YK

    X

    )SS(Yln

    )XYS(

    XYSYK

    m

    S

    m

    S =

    +

    +

    +++

    0000

    0

    00

    001

    (10)

    These rather unwieldy equations can be used to generate a graph showing the

    changes in biomass and substrate concentrations during the course of a batch

    fermentation (fig). Their main disadvantage is that they are not explicit in Xand Sso

    that a trial and error technique has to be used to determine their values at a

    particular value of t.

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    Manufacturing of Ethyl Alcohol from Fruit Waste

    Ethyl Alcohol by Fermentation

    Chemical reactions

    (a) Main reaction

    InvertaseC12H22O11 + H2O 2C6H12O6

    Zymase

    C6H12O6 2C2H5OH + 2CO2

    (b) Side reactions

    2C6H12O6 + H2O ROH + R' CHOhigher mol. Wt. Alcohols

    Quantitative requirements

    (a) Basis : 1 ton of 100% alcohol (1.26 kiloliters) and 90%

    yield from total sugar

    Molasses (50-55% total sugar) 5.6 tons

    Sulfuric acid (600 Be) 27 kg

    Ammonium sulfate 2.5 kg

    Coal 0.7-1.5 tons

    Process water 12 tons

    Cooling water 50 tons

    Electricity 35 KWH

    By-products : CO2 0.76 ton

    Fusel oil (higher mol. wt. Alcohols )

    Residual cattle feed or fertilizer 0.20 0.60 ton

    (b) Plant capacities : 10-100 tons/day of ethyl alcohol

    Process description

    Molasses is diluted to a 10-15% sugar concentration and adjusted to a pH of

    4-5 to support yeast growth which furnishes invertase and zymase catalyticenzymes. Nutrients such as ammonium and magnesium sulfate or phosphate is

    added when lacking in the molasses. This diluted mixture called mash is run into

    large wooden or steel fermentation tanks.

    Yeast solution, grown by inoculating sterile mash, is added and fermentation

    ensues with evolution of heat which is removed via cooling coils. The temperature

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    is kept at 20-300C over a 30-70 hr period, rising near the end of 35 0C. Carbon

    dioxide may be utilized as a by-product by water scrubbing and compressing;

    otherwise it is vented after water scrubbing.

    Separation of the 8-10% alcohol in the fermented liquor called beer is

    accomplished by a series of distillations. In the beer still, alcohol (50-60% conc.)

    and undesirable volatiles such as aldehydes are taken off the top and fed to the

    aldehyde still. Alcohol is pulled off as a side-stream split to the rectifying column. In

    this final column, the azeotropic alcohol-water mixture of 95% cannot is taken off as

    a top side streams conde and run to storage where it is split into three parts :

    (1) direct sale as potable, government controlled alcohol

    (2) denatured by small additions of mildly toxic ingredients and sold for industrialuses

    (3) made anhydrous by ternary azeotropic distillation using benzene or

    extractive distillation using ethylene glycol

    When fusel oil recovery is practiced, side-streams are drawn off near the bottom of

    the aldehyde and rectifying columns and are separated by decantation. These

    higher molecular weight alcohols are sold directly for solvents or are fractionated to

    give predominantly amyl alcohol.

    The bottoms from the beer still, known as slops, are either discharged as

    waste or concentrated by evaporation to cattle feed depending on fuel and by-

    product sales economics.

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    Major engineering problems Collection and storage of molasses

    Maintenance of sterile and specific yeast culture conditions.

    Batch versus continuous operation; continuous molasses dilution in the head

    end of the process and continuous distillation are incorporated to save

    space, equipment and operating costs

    Waste disposal problem : if uneconomic to concentrate for cattle feed, must

    use trickling filters, activated sludge or anaerobic digestion to lower the

    biological oxygen demand (BOD) before discharging to water run-off

    Fuel economy in the series of distillations : use of preheat exchangers

    Development of methods to produce anhydrous alcohol from the 95% alcohol

    azeotrope.

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    Alcohol from waste sulfite liquior.

    Figure gives a flow sheet of the Bellingham, Washington, plant. Removal of

    sulfur dioxide from the waste sulfite liquor is accomplished by stripping the liquor

    with stream, by countercurrent flow in a column, approximately 8 ft. in diameter by

    45 ft. tall, fabricated of stainless steel to the general pattern of a distillation column

    having 20 plates. Liquor enters at the top and steam at the bottom. Sulfur dioxide

    and steam are discharged out the top and are salvaged by injection into the digester

    cooking acid. The sulfur recovery amounts to about 20 lb.of sulfur per ton of pulp

    and offsets the cost of the steam required. The composition of the sulfite waste

    liquor discharged at the bottom varies depending on the stream input. Stripping

    results in complete removal of the free sulfur dioxide and part of the loosely

    combined sulfur dioxide. The pH of the stripped liquor varies between 3.8 and 4.2

    depending upon the grade of pulp being cooked. Although the column is equipped

    with control instruments to deliver automatically a product of constant pH, it is

    normally operated at a fixed steam liquor ratio of 1 lb of stream per 2 gal.of liquor

    feed. Part of the heat input is recovered in the digester cooking acid. The sulfite

    waste liquor from the base of the stripping column is pumped to the alcohol-plant

    building for continuation of liquor preparation.

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    The acidity of the sulfite waste liquor can be sufficiently reduced by stripping

    alone to make further treatment unnecessary, but for best economy it usually

    proves desirable to add lime. The lime is added as a 10% water slurry injected into

    the sulfite waste liquor at a point just ahead of the coolers. The equipment consists

    of an outside lime-storage bin, two agitated lime-slurry tanks, and the necessary

    pump. A pH controller regulates the amount of lime addition. The sulfite waste

    liquor is adjusted to a pH of 4.5 for fermentation. The quantity of lime average

    about 3 lb.of lime per 1000 gal.of sulfite waste liquor treated.

    After lime addition, the liquor is cooled to a temperature of 320C. Cooling is

    accomplished by two-stage flash evaporation under high vacuum, as this method

    has the advantage of concentrating the liquor at the same time that it is beingcooled and also of eliminating additional amounts of sulfur dioxide. Concentration is

    in the order of 12% which results in proportional reduction of costs during the

    subsequent steps of processing.

    The essential feature of this process is that after fermentation, the fermented

    work is run through a centrifugal separator to remove the yeast. This yeast is then

    re-used in a following fermentation in the operating cycle. The basis of this process

    is that when yeast is present in a suitable medium containing sugar, the course of

    the resulting fermentation tends to divide into two stages. In the first stage, the

    yeast cells multiply, using sugar for food, until they become crowded. During this

    stage there is maximum growth of yeast and minimum production of alcohol. In the

    second stage, the yeast reduces its rate of budding, or division, and continues to

    feed on the remaining sugar present. During this stage there is minimum growth of

    yeast and maximum production of alcohol. The purpose of re-using the yeast is to

    establish at once in each new fermentation the same high concentration of yeast

    cells that was present at the end of the previous fermentation. In this way the

    fermentation is limited to the second stage and the alcohol yield, therefore, is

    improved.

    Under any given set of conditions there is a fairly narrow concentration range

    of yeast cells per unit volume above which the rate of yeast growth diminishes every

    rapidly. Operation throughout the entire fermenting cycle at yeast concentration in

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    excess of such critical value offers important advantages in the case of waste sulfite

    liquor. Since large volumes of fermenting liquor are involved, profile yeast growths

    must ensue before the critical concentration is reached if the initial inoculum is

    small. This yeast growth is obtained at the expense of sugar, which would

    otherwise produce alcohol. At the same time, because waste sulfite liquor is, at

    best, a dilute sugar solution, the sugar required for yeast growth represents a

    greater proportion of the total than in the case of more concentrated sugar solutions

    from molasses or grain. The advantages of the yeast re-use process in increasing

    alcohol yields are, therefore, much greater in the case of waste sulfite liquor than in

    application to the more conventional raw materials.

    Fermentation is carried out in eight interconnected fomenter of 90,000 galcapacity each. To the liquor being pumped from storage is injected measured

    proportionate amounts of urea and yeast. The liquor enters the first fomenter,

    overflows into the second and so on through to the last fomenter whereupon

    fermentation is complete. From 70 to 80% of the fermentable sugars are fermented

    in the first two fomenters and about 95% of the fermentable sugars are converted to

    alcohol in the complete cycle. Fermentation time has been varied between 12 and

    20 hours. This short fermentation time, principally due to the elimination of the

    yeast-multiplication stage, can also be attributed partly to the adequate mixing

    provided in the fermenters, which keeps the yeast cells in suspension and partly to

    the fact that the yeast is acclimatized through re-use.

    Control of fermentation consists of regular measurement of the sugar

    concentration of the liquor entering and leaving the fermented and the alcohol

    content of the fermented liquor. The yeast is examined daily under the microscope

    for viability and cell count.

    From starch substrate

    Technology for manufacturing alcohol from starch based raw materials such

    as grains (sorghum grains) on laboratory scale which is scaled up to 15,000 LPD

    pilot plant, the process involved in brief is as follows: The chemical equation which

    takes place is as follows:

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    (C6H10O5)n + H2O > n(C6H1206)Starch glucose water Free glucose

    C6H12O6 > 2(C2H5OH) + 2CO2Glucose Ethanol Carbon dioxide

    A) Milling and Gelatinization

    The starch containing amylaceous material is first cleaned, purified, dried

    and milled/ground in small particle and then charged into a steam chest where it is

    cooled by steam at 140C and then enzymes are added. The steam injection

    breaks down the starch and make it more water soluble. The starch swells to many

    times the original size and become gelatinized. A liquefying enzyme also breaks the

    starch into smaller molecular chain.B ) Hydrolysis and saccharification

    The mash is then blown into a flash tank and cooled at around 90C. The

    sudden expansion dissolves the starch out of it bond and disengages it so that it

    can be decomposed more quickly and more completely. It is now ready for

    fermentation in mash tabs. Here the addition of appropriate enzymes i.e. -

    amylaze carries out composition of polysaccarides to the extent required under

    controlled condition.

    C) Fermentation

    The fermented mash of saccharides is then charged to pre-fermenter where

    yeast is added, (yeast is cultivated in a separate yeast culture vessel) The function

    of pre-fermenter is to allow the yeast cells to multiply and reduce the chances of

    bacterial contamination from t


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