LIQUID GLUCOSE FROM RICE
[CODE NO.3491]
Glucose is a commercially import ant product widely used by the food and pharmaceutical industries. In general, glucose is used in the food industry as a partial or complete substitute for sucrose. Glucose is the common name for the syrup which is used in large quantities in fruit canning, confectioneries, jams, jellies, preserves, ice cream, bakery products, pharmaceuticals, beverages and alcoholic fermentation. The functional purpose of glucose in the confectionery industry is to prevent crystallization of the sucrose while in the bakery products industry it is to supply fermentable carbohydrates. In the icecream and fruitpreserves, it used to increase the solidswithout causing an undue increase in the total sweetness. In pharmaceutical industry, glucose is used as a precursor to make vitamin C in the Reichstein process, to make citric acid, gluconic acid, polylactic acid and sorbitol. Currently, glucose is utilized as an intermediate raw material for bioethanol production.
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.
COST ESTIMATION
Plant Capacity : 70.00 MT/day
land & Building (24000 Sq.Mtr) : USD 27.94 Lacs
Plant & Machinery : USD 14.16 Lacs
Working Capital for 1 Month : USD 9.30 Lacs
Total Capital Investment : USD 54.83 Lacs
Rate of Return : 26%
Break Even Point : 55%
INTRODUCTION
STRUCTURE OF LACTOSE
TYPES OF GLUCOSE SYRUP
CONFECTIONER'S SYRUP
HIGH-MALTOSE GLUCOSE SYRUPS
MALTO DEXTRIN
DEALING WITH DE
PRODUCT DESCRIPTION AND USE
GLUCOSE AS ENERGY SOURCE IN LIVING CELL
CULINARY APPLICATIONS
HEALTH BENEFITS OF LIQUID GLUCOSE
LIQUID GLUCOSE USES IN FOODS
CHEMICAL AND PHARMACEUTICAL USES
OTHER INDUSTRIAL USES
USES AND APPLICATION OF MALTODEXTRIN
CALORIE REDUCTION
FROZEN ASSETS
SPORTS AND NUTRITION
PROPERTIES & CHARACTERISTICS
PROPERTIES OF STARCH
PHYSICAL PROPERTIES
CHEMICAL PROPERTIES
COMPOSITION OF RICE
COMPOSITION OF RAW AND PARBILED RICE.
CHEMICAL COMPOSITION OF DIFFERENT KINDS OF RICE
PROPERTIES AND CHARACTERISTICS OF MALTODEXTRIN
SACCHARIDE COMPOSITION OF COMMERCIAL MALTODEXTRINS
MARKET SURVEY (GLOBAL)
PRESENT MANUFACTURERS/SUPPLIERS
SPECIFICATIONS
SPECIFICATION FOR LIQUID GLUCOSE
COLOUR
REQUIREMENTS FOR LIQUID GLUCOSE (ALL GRADES)
COMMERCIAL PRODUCTION OF GLUCOSE
SUBSTRATE FOR GLUCOSE PRODUCTION
SEQUENCES IN GLUCOSE PREPARATION
MANUFACTURING PROCESS OF LIQUID GLUCOSE BY ACID HYDROLYSIS
PROCESS FLOW DIAGRAM
MANUFACTURING PROCESS FOR LIQUID GLUCOSE
RAW MATERIALS
CONFECTIONERY GLUCOSE-D:
LOW CONVERSION:
REGULAR CONVERSION
INTERMEDIATE CONVERSION
HIGH CONVERSION
PROCESS FLOW DIAGRAM OF LIQUID GLUCOSE
USING STARCH
MANUFACTURING PROCESS OF LIQUID GLUCOSE USING ENZYME HYDROLYSIS
FILTERATION OF LIQUID GLUCOSE
GENERAL INFORMATION
EQUIPMENT DESIGN
PURIFICATION OF GLUCOSE SYRUPS USING ACTIVATED CARBON
STANDARD DESIGN CONDITIONS
PROCESS FLOW DIAGRAM
MANUFACTURING PROCESS OF RICE STARCH
ALKALI STEEPING PROCESS:
SEPARATION OF THE STARCH:
CRYSTALLIZING AND DRYING 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
GENERAL PROCESS FLOW FOR STARCH DERIVED SWEETENERS.
TYPICAL CARBOHYDRATE PROFILE OF COMMERCIAL MALTODEXTRIN
ACID-CATALYZED HYDROLYSIS
COMPOSITION OF TYPICAL STARCH DERIVED SWEETERS
TYPICAL ACID CONVERTER.
CARBON TREATMENT AND REGENERATION SYSTEM
ACID–ENZYME PROCESSES
SYRUP DEMINERALIZATION SEQUENCE.
MULTIPLE EFFECT EVAPORATOR
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
OVERVIEW OF ANIMAL FEED INDUSTRY
OPTIMIZATION OF BYPRODUCT OF THE PROCESS (GLUTEN)
EQUIPMENT FOR MAKING CATTLE FEED PELLETS
DISCRIPTION OF PLANT & MACHINERY
RAW MATERIALS & YIELD
CONSULTANTS FOR GLUCOSE PLANT
SUPPLIERS OF BROKEN RICE
SUPPLIERS OF PLANT & MACHINERY (IMPORTED)
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