Commonly, glucose is prepared commercially via the enzymatic hydrolysis of starchinstead of acid hydrolysis. Many crops can be used as the source of the initial starch. Maize, rice, wheat, potato, cassava, arrowroot and sago are all used in various parts of the world. Nevertheless, using the starch needs to compete with their primary use as food crops. Due to the abundant of nonfood energy crops like cellulosic material, they are use to reduce the utilization of starch as raw material for production of glucose. Cellulosic materials including agricultural, agroindustrial and forestry lignocellulosic residues have potential as cheap and renewable feedstocks for large scale production of fuels and chemicals. Currently, bioprocessing of lignocellulosics is focused on enzymatic hydrolysis of the cellulose fraction to glucose, followed by fermentation to fuelgrade ethanol. However, enzymatic hydrolysis of cellulosic materials to produce fermentable sugars has also enormous potential in meeting global food and energy demand via biological route.

In lignocellulosic materials cellulose is physically associated with hemicellulose and physically and chemically associated with lignin. The presence of these two fractions is reported to make the access of cellulase enzymes to cellulose difficult, thus reducing the efficiency of the hydrolysis. There are several kinds of pretreatment able to disrupt the lignocellulosic structure for increasing the efficiency of the hydrolysis which have been investigated but are not within the scope of this study. However, the effect of temperature and pH are also significant in cellulose hydrolysis which will be stud ying in this study. The temperature and pH influence the efficiency of cellulase to degrade the cellulose for producing glucose.

In order to produce glucose, cellulose is essential to break it down first.By using acid hydrolysis, conversion of cellulose to glucose only produces low glucose concentration because acid is no selectivity. Furthermore, by using acid causes the cost production of glucose is highdue to demand of neutralization after hydrolysis which can contribute to corrosion problem if there is no neutralization process. Other that, the need of high temperature during acid hydrolysis process also contribute s to the cost of production because high energy is consumed. Waste from acid hydrolysis also gives the bad effect to the environment which is using high concentration of acid can cause harmful to the environment. Therefore, the investigation attempted to determine the glucose production by using enzymatic hydrolysis process inorder to replace acid hydrolysis process.

Nevertheless by using enzymatic hydrolysis need highly specific and very sensitive. Their environmental condition such temperature and pH influence the activity of the enzymes in the system. Hence, the effect of temperature and pH is investigated to determine the maximum conditions of enzymatic hydrolysis process in glucose production.

Glucose is a simple monosaccharide sugar also known as grape sugar, blood sugar or corn sugar which is a very important carbohydrate in biology. The living cell uses it as a source of energy and metabolic intermediate. Glucose is one of the main products of photosynthesis and starts cellular respiration in both prokaryotes and eukaryotes. Glucose (C6H12O6) contains six carbon atoms, one of which is part of an aldehyde group (Figure). Therefore, glucose is an aldohexose. Glucose is commonly available in the form of a white powder or as a solid crystal, called dextrose. It can also be dissolved in water as an aqueous solution, glucose syrups.

Its solubility level is very high.

Glucose can be forms disaccharide when two of monosaccharide are linked together such sucrose, the combination of glucose with fructose. Sucrose is the most common sweetener in the modern, industrialized world, although it has been displaced in industrial food production by some other sweeteners such as glucose syrups or combinations of functional ingredients and high intensity sweeteners.

In lactose, another important disaccharide, glucose is joined to galactose (Figure ). It used as the predominant sugar in milk. For maltose, a product of starch digestion is glucose glucose disaccharide. Glucose also can be forms polysaccharides when the units (either mono or disaccharides) are repeated and joined together by glycosidic bonds like cellulose. Cellulose is yet a third polymer of the monosaccharide glucose.

Structure of Lactose

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Commonly, glucose is prepared commercially via the enzymatic hydrolysis of starchinstead of acid hydrolysis. Many crops can be used as the source of the initial starch. Maize, rice, wheat, potato, cassava, arrowroot and sago are all used in various parts of the world.Nevertheless, using the starch needs to compete with their primary use as food crops. Due to the abundant of nonfood energy crops like cellulosic material, they are use to reduce the utilization of starch as raw material for production of glucose. Cellulosic materials including agricultural, agroindustrial and forestry lignocellulosic residues have potential as cheap and renewable feedstocks for large scale production of fuels and chemicals. Currently, bioprocessing of lignocellulosics is focused on enzymatic hydrolysis of the cellulose fraction to glucose, followed by fermentation to fuelgrade ethanol. However, enzymatic hydrolysis of cellulosic materials to produce fermentable sugars has also enormous potential in meeting global food and energy demand via biological route.

The post LIQUID GLUCOSE FROM RICE appeared first on EIRI - eBooks and Project Reports.

Commonly, glucose is prepared commercially via the enzymatic hydrolysis of starchinstead of acid hydrolysis. Many crops can be used as the source of the initial starch. Maize, rice, wheat, potato, cassava, arrowroot and sago are all used in various parts of the world.Nevertheless, using the starch needs to compete with their primary use as food crops. Due to the abundant of nonfood energy crops like cellulosic material, they are use to reduce the utilization of starch as raw material for production of glucose. Cellulosic materials including agricultural, agroindustrial and forestry lignocellulosic residues have potential as cheap and renewable feedstocks for large scale production of fuels and chemicals. Currently, bioprocessing of lignocellulosics is focused on enzymatic hydrolysis of the cellulose fraction to glucose, followed by fermentation to fuelgrade ethanol. However, enzymatic hydrolysis of cellulosic materials to produce fermentable sugars has also enormous potential in meeting global food and energy demand via biological route.

In lignocellulosic materials cellulose is physically associated with hemicellulose, and physically and chemically associated with lignin. The presence of these two fractions is reported to make the access of cellulase enzymes to cellulose difficult, thus reducing the efficiency of the hydrolysis. There are several kinds of pretreatment able to disrupt the lignocellulosic structure for increasing the efficiency of the hydrolysis which have been investigated but are not within the scope of this study. However, the effect of temperature and pH are also significant in cellulose hydrolysis which will be stud ying in this study. The temperature and pH influence the efficiency of cellulase to degrade the cellulose for
producing glucose.

In order to produce glucose, cellulose is essential to break it down first.By using acid hydrolysis, conversion of cellulose to glucose only produces low glucose concentration because acid is no selectivity. Furthermore, by using acid causes the cost production of glucose is highdue to demand of neutralization after hydrolysis which can contribute to corrosion problem if there is no neutralization process . Other that, the need of high temperature during acid hydrolysis process also contribute s to the cost of production because high energy is consume d. Waste from a cid hydrolysis also gives the bad effect to the environment which is using high concentration of acid can cause harmful to the environment. Therefore, the investigation attempted to determine the glucose production by using enzymatic hydrolysis process inorder to replace acid hydrolysis process.

Nevertheless by using enzymatic hydrolysis need highly specific and very sensitive. Their environmental condition such temperature and pH influence the activity of the enzymes in the system. Hence, the effect of temperature and pH is investigated to determine the maximum conditions of enzymatic hydrolysis process in glucose production.

INTRODUCTION
TYPES OF GLUCOSE SYRUP
PRODUCT DESCRIPTION AND USE
USES AND APPLICATION OF MALTODEXTRIN
PROPERTIES & CHARACTERISTICS
CHEMICAL COMPOSITION OF DIFFERENT KINDS OF RICE
PROPERTIES AND CHARACTERISTICS OF MALTODEXTRIN
B.I.S. SPECIFICATION
OVERVIEW AND AVAILABILITY OF RICE IN INDIA
MARKET SURVEY
IMPORT DATA OF LIQUID GLUCOSE
EXPORT DATA OF LIQUID GLUCOSE
PRODUCTION OF LIQUID GLUCOSE IN INDIA
MARKET SURVEY (GLOBAL)
PRESENT MANUFACTURERS
SPECIFICATIONS
COMMERCIAL PRODUCTION OF GLUCOSE
SEQUENCES IN GLUCOSE PREPARATION
MANUFACTURING PROCESS OF LIQUID GLUCOSE BY ACID HYDROLYSIS
PROCESS FLOW DIAGRAM
MANUFACTURING PROCESS FOR LIQUID GLUCOSE
PROCESS FLOW DIAGRAM OF LIQUID GLUCOSE
USING STARCH
MANUFACTURING PROCESS OF LIQUID GLUCOSE USING
ENZYME HYDROLYSIS
FILTERATION OF LIQUID GLUCOSE
PURIFICATION OF GLUCOSE SYRUPS USING ACTIVATED CARBON
PROCESS FLOW DIAGRAM
MANUFACTURING PROCESS OF RICE STARCH
MANUFACUTRING PROCESS OF MALTODEXTRIN FROM BROKEN RICE
PROCESS FLOW DIAGRAM OF MALTODEXTRIN FROM RICE STARCH
OBTAINED
FROM BROKEN RICE
TECHNICAL DETAILS AND OBTIMIZATION OF LIQUID
GLUCOSE AND MALTO DEXTRIN
SEPARATION OF PROTEINS AND PRODUCTION OF MALTODEXTRIN
ASSAY METHOD OF MALTO DEXTRIN (REDUCING SUGAR)
WET MILLING PROCESS
TECHNICAL PARAMETER IN LIQUID GLUCOSE PLANT
ENZYMES PROCUREMENT ANALYSIS DETAILS OF ALPHA
AMYLASE ENZYMES
MATERIAL SAFETY DATA SHEET FOR ALPHA AMYLASE ENZYMES
OVEVIEW OF ANIMAL FEED INDUSTRY
OPTIMIZATION OF BYPRODUCT OF THE PROCESS (GLUTEN)
RAW MATERIALS & YIELD
CONSULTANTS FOR GLUCOSE PLANT
SUPPLIERS OF RAW MATERIALS
SUPPLIERS OF BROKEN RICE
SUPPLIERS OF PLANT & MACHINERY (IMPORTED)
LIST OF THE BUYERS OF LIQUID GLUCOSE

APPENDIX – A :

1. COST OF PLANT ECONOMICS
2. LAND & BUILDING
3. PLANT AND MACHINERY
4. FIXED CAPITAL INVESTMENT
5. RAW MATERIAL
6. SALARY AND WAGES
7. UTILITIES AND OVERHEADS
8. TOTAL WORKING CAPITAL
9. COST OF PRODUCTION
10. PROFITABILITY ANALYSIS
11. BREAK EVEN POINT
12. RESOURCES OF FINANCE
13. INTEREST CHART
14. DEPRECIATION CHART
15. CASH FLOW STATEMENT
16. PROJECTED BALANCE SHEET

The post LIQUID GLUCOSE FROM BROKEN RICE appeared first on EIRI - eBooks and Project Reports.

Starch is a group of polysacchrides, composed of glucopyranose units joined together by-glucosidric linkages. It conforms to the molecular formula, (C6-H10O5)u, where n varies from a few hundred to over one million. Starch is found as the reserve carbonhydrate in various parts of plants and is enzymatically broken down to gluose to other erbohydrates according to the metabollic needs of the plants.

Industrially, starch is broadly divided into two types viz, natural and modified. Natural starches, also designated as unmodified starches or simply starches, are obtained from grains such as and sorghum. from roots like potato, tapioca and arrow root, and from the pith of the stems of certain palms such a sago. They are further classified into cereal starches and root starches. The characteristics of the natural starches are changed by chemical or enzymatic action and the products of these reactions are termed modified starches. This group includes dextrins, acid-modified starches, oxidized starches, starch esters, starch ethers, dialdehyde starches, and cationic starches.

INTRODUCTION
PRODUCT DESCRIPTION AND USE
USES AND APPLICATION OF MALTODEXTRIN
PROPERTIES & CHARACTERISTICS
PROPERTIES AND CHARACTERISTICS OF MALTODEXTRIN
B.I.S. SPECIFICATION
OVERVIEW AND AVAILABILITY OF RICE IN INDIA
MARKET SURVEY
IMPORT DATA OF LIQUID GLUCOSE
EXPORT DATA OF LIQUID GLUCOSE
PRODUCTION OF LIQUID GLUCOSE IN INDIA
INSTALLED CAPACITY, PRODUCTION AND CAP. UTILIZATION OF LIQUID GLUCOSE
ESTIMATED DEMAND
MARKET SURVEY (GLOBAL)
OVERVIEW OF RICE IN SURINAME
RICE PRODUCTION (MILLED) IN SURINAME
FUTURE EXPANSION PLANNING OF KBRL LTD INTO LIQUID GLUCOSE
PRESENT MANUFACTURERS
SPECIFICATIONS
MANUFACTURES OF STARCH AND ALLIED PRODUCTS
MANUFACTURING PROCESS
PROCESS FLOWSHEET FOR STARCH MANUFACTURING
FROM BROKEN RICE
MANUFACTURING PROCESS FOR LIQUID GLUCOSE
MANUFACTURING DIAGRAM MANUFACTURS OF LIQUID GLUCOSE
MANUFACTURING PROCESS OF LIQUID GLUCOSE FROM BROKEN
RICE USING ENZYME HYDROLYSIS
PROCESS FLOW DIAGRAM
MANUFACUTRING PROCESS OF MALTODEXTRIN FROM BROKEN RICE
PROCESS FLOW DIAGRAM OF MALTODEXTRIN FROM RICE STARCH OBTAINED FROM BROKEN RICE
SEPARATION OF PROTEINS AND PRODUCTION OF MALTODEXTRIN
ASSAY METHOD OF MALTO DEXTRIN (REDUCING SUGAR)
WET MILLING PROCESS
RAW MATERIALS & YIELD
CONSULTANTS FOR GLUCOSE PLANT
SUPPLIERS OF RAW MATERIALS
COMPLETE PLANT SUPPLIERS FOR LIQUID GLUCOSE
SUPPLIERS OF BROKEN RICE
SUPPLIERS OF PLANT & MACHINERY
WHAT IS THE PURPOSE OF USING LIQUID GLUCOSE WHILE MAKING CHOCOLATES?
LIST OF THE BUYERS OF LIQUID GLUCOSE

APPENDIX – A :

1. COST OF PLANT ECONOMICS
2. LAND & BUILDING
3. PLANT AND MACHINERY
4. FIXED CAPITAL INVESTMENT
5. RAW MATERIAL
6. SALARY AND WAGES
7. UTILITIES AND OVERHEADS
8. TOTAL WORKING CAPITAL
9. COST OF PRODUCTION
10. PROFITABILITY ANALYSIS
11. BREAK EVEN POINT
12. RESOURCES OF FINANCE
13. INTEREST CHART
14. DEPRECIATION CHART
15. CASH FLOW STATEMENT
16. PROJECTED BALANCE SHEET

The post LIQUID GLUCOSE FROM BROKEN RICE Cap: 20,000 Ton/Annum appeared first on EIRI - eBooks and Project Reports.

Starch is a group of polysacchrides, composed of glucopyranose units joined together by-glucosidric linkages.  It conforms to the molecular formula, (C6-H10O5)u, where n varies from a few hundred to over one million.

Starch is found as the reserve carbonhydrate in various  parts of plants  and is enzymatically broken down to gluose to  other  erbohydrates according to the metabollic needs of the plants.

Industrially, starch is broadly divided into two  types viz, natural and modified. Natural starches, also designated as unmodified starches or simply starches, are obtained from  grains such as and sorghum. from roots like potato, tapioca and  arrow root, and  from the pith of the stems of certain palms such a sago. They are further classified into cereal starches and root starches.

The characteristics of the natural starches are changed by chemical or enzymatic action and the products of these reactions are termed modified starches. This  group  includes dextrins,  acid-modified starches,  oxidized  starches, starch esters, starch ethers, dialdehyde starches, and cationic starches.

PROJECT REPORT COVERS:

•     Introduction
•     Uses and Applications
•     Properties
•     Market Survey with future aspects
•     Present Manufacturers
•     B.I.S. Specifications
•     Manufacturing Process with Formulae
•    Cost Economics with Profitability Analysis
•     Capacity
•     Land & Building Requirements with Rates
•     List & Details of Plant and Machinery with their Costs
•     Raw Materials
•     Details/List and Costs
•     Power & Water Requirements
•     Labour/Staff Requirements
•     Utilities and Overheads
•     Total Capital Investment
•     Turnover
•     Cost of Production
•     Break Even Point
•     Profitability
•     Land Man Ratio
•     Suppliers of Plant & Machineries and Raw Materials.

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Potato  is  widely consumed as food all over the  world.  It contains  the  starch as a major carbohydrate. Surplus  and  cull potatoes are used as feed for live stock and also as raw material for  the  manufacture of starch, ethyl alcohal and a few other industrial products like, dextrose, liquid Glucose etc.

The  potato contains approximately 18-21% of  carbohydrates. The  major carbohydrate is starch. This starch is comprising  65-80%  of  the dry weight of the tuber, is calorifically the most important nutritional component. In the raw tuber , it is present as  microscopic granules in levcoplasts lining the interior  cell walls of parenchyma tissue. The granule is ellipsoidal in  shape, 100N*60N,  with striations like an oyster shell. Under  polarized light,  the  granule  shows an irregular  black  cross.  Electron micrographs  reveal  a surprising smooth surface  structure.  The ratio  of amylase to amylopectine in potato starch is  24:76  and the  gelatinization  temperature ranges from 56oC  to  69oC  with water  this starch forms a translucent paste of  high  viscosity. Freshly  harvested  mature tubers contain more  sugars  than  the large ones. A slight rise in total sugars is observed when tubers are stored at 20-30oC. However when the storage temperature is 4o or less., the total reducing sugars increase, the rate and extent of increase being greater when lower the temperature down to  the freezing  point.  The maximum sugar concentration (3 to  10%)  is reached after 4-8 weeks.

PROJECT REPORT COVERS:

•     Introduction
•     Uses and Applications
•     Properties
•     Market Survey with future aspects
•     Present Manufacturers
•     B.I.S. Specifications
•     Manufacturing Process with Formulae
•    Cost Economics with Profitability Analysis
•     Capacity
•     Land & Building Requirements with Rates
•     List & Details of Plant and Machinery with their Costs
•     Raw Materials
•     Details/List and Costs
•     Power & Water Requirements
•     Labour/Staff Requirements
•     Utilities and Overheads
•     Total Capital Investment
•     Turnover
•     Cost of Production
•     Break Even Point
•     Profitability
•     Land Man Ratio
•     Suppliers of Plant & Machineries and Raw Materials.

The post LIQUID GLUCOSE FROM POTATOES appeared first on EIRI - eBooks and Project Reports.

Starch,  the most abundant carbohydrate obtained from  plant kingdom, is the starting raw material for making Liquid  Glucose. Starch is commonly produced from corn, millets and tubers;  which grows proliferously in sub-tropical countries. Starch is isolated from the plant source as an aqueous suspension of pure  granules. In  developed  and  developing countries,  separation  of  starch granules  from the aqueous suspension is done in a  sophisticated way  involving  high investment. In India,  although  the  starch production  from the various sources is mostly confined to  small scale sector/cottage industries, some of the big industries  also separate starch for their captive consumption.

PROJECT REPORT COVERS:

•     Introduction
•     Uses and Applications
•     Properties
•     Market Survey with future aspects
•     Present Manufacturers
•     B.I.S. Specifications
•     Manufacturing Process with Formulae
•    Cost Economics with Profitability Analysis
•     Capacity
•     Land & Building Requirements with Rates
•     List & Details of Plant and Machinery with their Costs
•     Raw Materials
•     Details/List and Costs
•     Power & Water Requirements
•     Labour/Staff Requirements
•     Utilities and Overheads
•     Total Capital Investment
•     Turnover
•     Cost of Production
•     Break Even Point
•     Profitability
•     Land Man Ratio
•     Suppliers of Plant & Machineries and Raw Materials.

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