OLEORESIN EXTRACTION PLANT FROM CHILLIS [CODE NO.3665]
Oleoresins are the concentrated liquid form of the spice. They are obtained from spices by extraction with a non-aqueous solvent followed by removal of the solvent by evaporation. This spice derivative has the same character and property of the spice it is obtained from. They reproduce the character of the respective spice and spice oil fully. Spice oleoresins represent the complete flavour profile of the spice. It contains the volatile as well as nonvolatile constituents of spices. Oleoresins can replace whole/ground spices without impairing any flavour and aroma characteristic. Spice oleoresins guarantee superior quality of flavour and aroma. They are complete and balanced, consistent, and standardised. The quality of an oleoresin is typically evaluated on the basis of presence of the active ingredients in desired levels. As these are concentrated extracts, they are typically used as a diluted dispersion plated on a neutral dry carrier or as a diluted blend in a solubilizing medium such as vegetable oil to match the desired strength of the ground spice/herb. All the spices contain essential oils in varying proportions which can be extracted by steam distillation.
The main products in a spice oleoresin plant are oleoresins of chilli, pepper, ginger and turmeric. The co-products are corresponding spice oils, which are widely used in food and pharmaceutical industries. Spent meals of spice powders after oleoresin extraction are by-products and are devoid of essential oils, pungent principles, fixed oils and resinous matter for which the spices are valued. This may be considered for incorporation in animal feed formulations, as spent meal is rich in carbohydrate and cellulose.
COST ESTIMATION
Plant Capacity 28480 Ltr/Year
Land & Building Rs. 1.57 Cr
Plant & Machinery Rs. 3.02 Cr
Working Capital for 1 Month Rs. 1.27 Cr
Total Capital Investment Rs. 6.44 Cr
Rate of Return 39%
Break Even Point 46%
INTRODUCTION
WHY OLEORESINS?
TECHNOLOGY
ADVANTAGES & DISADVANTAGE OF OLEORESINS
THE ADVANTAGES OF OLEORESINS
ADVANTAGES & DISADVANTAGE
ADVANTAGES OF SCFE
ADVANTAGE OF CO2 AS A SOLVENT
RAW MATERIALS
BOTANICAL DESCRIPTION
NUTRITIONAL VALUE OF CHILLI
USES
INDIAN NAME OF SPICES
FOREIGN NAME OF SPICES
INDIAN CHILLI VARIETIES
DIFFERENT VARIETIES
BIRDS EYE CHILLI (DHANI)
BYADAGI (KADDI)
ELLACHIPUR SANNAM-S4 TYPE
GUNTUR SANNAM-S4 TYPE
HINDPUR-S7
JWALA
KANTHARI-WHITE
KASHMIR CHILLI
MADHYA PRADESH G.T.SANNAM
METHODS OF OLEORESIN EXTRACTION
SOLVENT EXTRACTION PROCESS
SUPERCRITICAL FLUID EXTRACTION PROCESS
STEAM DISTILLATION PROCESS
SCF MANUFACTURING PROCESS
SAMPLE PREPARATION
SUPERCRITICAL FLUID EXTRACTION (SFE)
SCF TECHNOLOGY DEVEN SUPERCRITICALS PVT. LTD., INDIA
SPECIAL FEATURES ON OUR SCFE SYSTEM
PLC BASED CONTROL SYSTEM
INSTRUMENTATION
PROPERTIES OF SCF
PHASE DIAGRAM
COMPARISON OF SUPERCRITICAL CO2 FLUID EXTRACTION (SCFE)
AND CHEMICAL EXTRACTION
SFE ADVANTGE OVER OTHER PROCESS
SUPERCRITICAL FLUID EXTRACTION TECHNOLOGY AND ITS APPLICATION
IN FOOD INDUSTRY
PRINCIPLE AND INFLUENCING FACTORS
THE BASIC PRINCIPLE OF SUPERCRITICAL FLUID EXTRACTION
FACTORS INFLUENCING SUPERCRITICAL FLUID EXTRACTION
RAW MATERIALS
SOLUBILITY (TEMPERATURE AND PRESSURE)
APPLICATION STATUS AND PROGRESS
PROPERTIES OF OLEORESIN
PHYSICAL PROPERTIES TO BE CHECKED
EFFECT OF PH STABILITY OF NATURAL OLEORESIN EXTRACTED
BY SUPERCRITICAL CO2
HEAT STABILITY OF OLEORESIN EXTRACTED BY SUPERCRITICAL CO2
TEM OF OLEORESIN NANOPARTICLES EXTRACTED BY SUPERCRITICAL CO2
TEM OF OLEORESIN NANOPARTICLES EXTRACTED BY SUPERCRITICAL CO2
STANDARD CURVE OF OLEORESIN
FT-IR ANALYSIS OF OLEORESIN
PH STABILITY OF NATURAL OLEORESIN EXTRACTED BY SUPERCRITICAL CO2
HEAT STABILITY OF OLEORESIN EXTRACTED BY SUPERCRITICAL CO2
DSC OF NANO OLEORESIN
VARIOUS OLEORESINS & THEIR APPLICATIONS
SOLVENTS
MARKET POTENTIAL
SPICE OILS AND OLEORESINS MARKET SEGMENTATION
INDIA DOMINATES GLOBAL MARKET FOR SPICE OLEORESIN AS DEMAND
FOR NATURAL AGENTS’ SWELLS
SEGMENTATION
KEY PLAYERS
REGIONAL MARKET SUMMARY
GLOBAL OLEORESINS MARKET SHARE (%), BY REGION, 2017
GLOBAL OLEORESINS MARKET, BY PRODUCT
GLOBAL OLEORESINS MARKET, BY RAW MATERIAL
GLOBAL OLEORESINS MARKET, BY APPLICATION
GLOBAL OLEORESINS MARKET, BY REGION
"RISING DEMAND FOR PACKAGED SPICES AND SEASONING IN RESTAURANTS"
"PAPRIKA OLEORESIN HELD OVER ONE THIRD OF THE REVENUE SHARE IN 2015"
"FLAVOR WAS THE LARGEST APPLICATION SEGMENT IN 2015"
"EUROPE HELD OVER ONE-THIRD OF REVENUE SHARE IN 2015"
"FEW COMPANIES HOLD A LARGE MARKET SHARE OF THE OVERALL OUTPUT"
THE GLOBAL OLEORESIN MARKET IS CONCENTRATED IN NATURE WITH FEWER COMPANIES HOLDING A MAJOR SHARE IN THE INDUSTRY. THE GLOBAL INDUSTRY IS EXPECTED TO WITNESS AN INCREASE IN MERGERS, ACQUISITIONS AND STRATEGIC ALLIANCES OVER THE NEXT SEVEN YEARS.
MAJOR COMPANIES INCLUDE UNIVERSAL OLEORESINS, UNGERER & COMPANY,
PLANT LIPIDS, AKAY, SYNTHITE, AVT NATURAL PRODUCTS LTD, INDO WORLD,
PAPRIKA OLEO’S, PARAS PERFUMERS, AMBE GROUP, ASIAN OLEORESIN
COMPANY, CYMBIO PHARMA PVT LTD AND BIOPREX LABS.
OLEORESIN MARKET KEY DEVELOPMENTS
OLEORESIN MARKET MAJOR PLAYERS
EUROPE AN INTERESTING MARKET FOR OLEORESINS
EUROPEAN INDUSTRY INCREASINGLY USES FORMULAS WITH NATURAL
INGREDIENTS
ETHNIC FOODS ARE GAINING POPULARITY
SALT REDUCTION PROVES TO BE A CHALLENGE
REQUIREMENTS MUST OLEORESINS COMPLY WITH TO BE ALLOWED
ON THE EUROPEAN MARKET
QUALITY REQUIREMENTS
COLOUR AND FLAVOR
PURITY
INDIA DOMINATES THE OLEORESIN MARKET
BUYERS SHOW INTEREST IN NATURAL SUBSTITUTES
NEED FOR PRODUCT DISTINCTION
TWO MARKET SEGMENTS FOR OLEORESINS
TARGET IMPORTERS
EXPORTS TO FLAVOURING MANUFACTURERS
END-MARKET PRICES FOR OLEORESINS
VALUE ADDITION BY IMPORTERS
PRICE DEVELOPMENTS FOR SELECTED OLEORESINS, FOURTH QUARTER 2017
LABELLING & PACKAGING REQUIREMENTS
LABELLING
YOUR LABELS MUST INCLUDE
PACKAGING
PLANT & MACHINERY MANUFACTURER
CHILLI SUPPLIERS
RAW MATERIAL PHOTOGRAPHS
PRODUCT PHOTOGRAPHS
MACHINERY PHOTOGRAPHS
PRESSURE REGULATING EQUIPMENT
TRIPLEX PLUNGER PUMPS MAX. FLOW RATE OF 600 LTR/HR
CO2 PRESSURE INCREASE FROM 50 BAR TO 300 BAR
CO2 PASSED THROGH SUPER HEATER TO REACH A SUPER CRITICAL STATE
FOOD GRADE STAINLESS STEEL 316/304
SEPARATION OF UTILITY AREA AND CLEQN AREA EQUIPMENT
SCADA SYSTEM WITH ABILITY ADD NEW RECIPES
ACTIVE SYSTEM MONITORING FOR SAFETY AND RELIABILITY USING PRESSSURE GAUGES, PRESSURE TRANDUCERS
ADVANCED INTEGRATED CONTROLS AND COMMUNICATION
SPECIALLY DESIGNED HEAT EXCENGER TO OPTIMIZE DESIGN TEMPERATURE
THE CO2 IN SUPER CRITICAL STATE PASSES THROUGH THE EXTYRACTOR
AND CARRIES WIT IT THE ESSENTIAL OILS AND NATURAL EXTRACTS.
THE CO2 IN THE SEPARATPOR AT LOWER PRESSURE TURNS IN TO A GAS AND THE EXTRACT IS SEPARATED DUE TO THE GAS LIQUID SEPARATION.
APPENDIX – A:
01. PLANT ECONOMICS
02. LAND & BUILDING
03. PLANT AND MACHINERY
04. OTHER FIXED ASSESTS
05. FIXED CAPITAL
06. RAW MATERIAL
07. SALARY AND WAGES
08. UTILITIES AND OVERHEADS
09. TOTAL WORKING CAPITAL
10. TOTAL CAPITAL INVESTMENT
11. COST OF PRODUCTION
12. TURN OVER/ANNUM
13. BREAK EVEN POINT
14. RESOURCES FOR FINANCE
15. INSTALMENT PAYABLE IN 5 YEARS
16. DEPRECIATION CHART FOR 5 YEARS
17. PROFIT ANALYSIS FOR 5 YEARS
18. PROJECTED BALANCE SHEET FOR (5 YEARS)
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