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SUPERCRITICAL FLUID EXTRUSION (SCFX)
PRAGATI SINGHAM
Roll No.- 10703
Ph.D 1st year
CONTENTS
CASE STUDIES
CONCLUSION
FUTURE THRUSTS
INTRODUCTION
INTRODUCTION
High temperature
High shear
Steam puffing
Extrusion Technology
Disadvantages
High solubilizing capacity
High Diffusivity
Low temperature process
Supercritical Fluid CO2
Advantages
Supercritical Fluid Extrusion
SUPERCRITICAL FLUID EXTRUSION
(SCFX)
Versatile
High production Rate
Low temperature
Low shear
High expansion
SUPERCRITICAL FLUID EXTRUSION PROCESS
(SCFX)
•
Development of
gas holding
rheological
properties
Injection of
CO2
Nucleation
of Cells
Expansion
OBJECTIVE
To develop novel extrusion protocols to directly incorporating
fruit/dairy by-products into shelf-stable, puffed, extruded
products and evaluate changes in their quality due to processing.
MATERIALS AND METHODS
Materials
Pre-gelatinized starch 76%
Apple pomace powder (22% & 28%)
Lecithin 1%
Distilled monoglycerides, 1%
At 7.58 MPa
RESULTS
External
Internal
Nutrient Retention
 Direct utilization of apple pomace into nutrient-enriched,
shelf stable puffed extruded products
 Retention of 84% of the Total Phenolic Content (TPC) and
74% of the total antioxidants
 Low density extrudates 0.21-0.35 g/cm3 were obtained
INFERENCES
OBJECTIVE
To produce soy based expanded crisps fortified with
micronutrients and protein by using SCFX
MATERIAL AND METHODS
Lecithin (1.5g/100g),
Distilled monoglycerides (1g/100g),
Table Salt (1.5g/100g)
Micronutrient premix 325mg/100g
Flour % Soy protein Conc.
(RS SPC-25)
% Soy protein Conc.
(RS SPC-40)
% Soy flour
(RS SF-25)
% Soy flour
(RS SF-40)
Waxy rice flour
(WRF) (g/100g)
71.5 56.5 71.5 56.5
Rice-Soy Concentrate Crisps (A) 25% (B) 40% Rice-Soy Flour Crisps (A) 25% (B) 40%
0
0.1
0.2
0.3
RSC-SPC
25
RSC-SF 25 RSC-SPC
40
RSC-SF 40 RSC-SPC
25
RSC-SPC
40
RSC-SPC
40
RSC-SF 40
Piece Density (g/cm3) Bulk Density (g/cm3)
0
1
2
3
4
5
RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40
Expansion Ratio (%)
Density
Expansion
Ratio
RESULTS
-0.6
-0.4
-0.2
0
0.2
0.4
0.6
0.8
RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40
a value
59
60
61
62
63
64
RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40
L value
0
4
8
12
16
RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40
b value
COLOR
0
2000
4000
6000
8000
10000
12000
RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40
Vitamin A (IU/100g)
Before Extrusion
After Extrusion
0
20
40
60
80
100
120
140
160
RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40
Vitamin C (mg/100g)
Before Extrusion
After Extrusion
MICRONUTRIENTS
RSC-SPC 25 was found to be best among the samples
Improved amino acid balance due to incorporation of soy
protein to rice flour
No undesirable quality attributes on fortification of vitamin A,
C and minerals.
Effective process based nutrient fortification approach to
reduce malnutrition.
INFERENCES
OBJECTIVE
To quantify the effects of die temperature, different levels of
alkalized cocoa powder and CO2 gas injection on cellular
structure and physical properties of extruded meal
MATERIAL AND METHODS
Corn meal
Variables
Temperature 95˚C, 110 ˚C and 120˚C
Alkalized cocoa powder (6% and 12%)
RESULTSSectionalExpansionIndex(SEI)
Effect of die temperature, ACP content and C02 gas injection
EXPANSION INDEX PIECE DENSITY
0%
6%
12%
ACP 95˚C 110˚C 120˚C 95˚C 110˚C 120˚C
DIE TEMPERTURE
CELL STRUCTURE
Without CO2 injection With CO2 injection
Die temperature, Alkalized Cocoa powder (ACP) content and
CO2 injection significantly affected the physical properties of
the extrudates
Addition of ACP imparted rigidity to the extruded structure
and reduced shrinkage
Uniform microcellular structure with reduced breaking
strength in ACP added CO2 injection process
INFERENCES
OBJECTIVE
To develop SCFX leavened dough and breads with density
comparable to the density of conventionally yeast-leavened
breads and commercial bread products
MATERIAL AND METHODS
Dough Formulae
Percentage Flour Weight
Ingredients Formula 1 Formula 2 Formula 3
Guar Gum 0.5 0.15 Nil
Egg powder 1 0.5 Nil
Ascorbic acid 0.01 0.2 0.2
Conventional baking
180˚C for 30 min
Combined Vacuum and
Conventional 188 ˚C with
50.8kPa vacuum for 30
min followed by 180 ˚C for
10 min.39 rpm
RESULTS
EXTERNAL MORPHOLOGY
0
0.1
0.2
0.3
0.4
0.5
C V+C C V+C C V+C
Formula 1 Formula 2 Formula 3
Bread Density (g/cm3)
0
10
20
30
40
C V+C C V+C C V+C
Formula 1 Formula 2 Formula 3
Crumb Moisture (%)
PHYSICO-CHEMICAL PROPERTIES
FORMULA 2 STALING TEST
Conventional
Baking
Combined
Conventional and
vacuum baking
Formula 2 yeast-free bread produced by combined
conventional vacuum baking using SCFX leavened dough was
found to be the best
Density and crumb hardness obtained in SCFX leavened
bread was comparable to yeast leavened breads
Bread quality was controllable as compared to conventional
yeast-leavened bread
Consistent ready-to-bake dough can be produced in shorter
time (approx. 0.36 to 0.41 h ) without ethanol emmission
INFERENCES
OBJECTIVE
To study the cross-linking of native/pre-gelatinized starch
blends and to create cross-linked microcellular starch foams by
reaction SCFX with STMP
MATERIAL AND METHODS
Samples:
Pre-gelatized wheat starch
Control mixture of native starch (40% w/w)and pre-gelatinized
starch (60% w/w)
Food-grade Sodium Trimetaphosphate (STMP): 9%
NaOH (0.1 M, 0.2 M)
SC-CO2: 0%, 1% and 1.5%
DENSITY and EXPANSION RATIO
RESULTS
EXTERNAL MORPHOLOGY
Yellowish
Bright white
Bright white
0
5
10
15
20
25
30
0% 1% 1.50%
SC-CO2 (% DRY FEED)
9% STMP 0.1 M NaOH
at 60˚C
9% STMP , 0.1 M NaOH
at 90˚C
0
2
4
6
8
10
12
0% 1% 1.50%
SC-CO2 (% DRY FEED)
9% STMP 0.2 M NaOH at
60˚C
9% STMP , 0.2 M NaOH
at 90˚C
WATER SOLUBILITY
Cross-linking, modified and integrated the structure of
extrudates
High pH, low temperature favoured restricted mobility which
leads to decrease in water solubility
pH played a key role in reactive supercritical fluid extrusion
Reactive Supercritical fluid extrusion can be successfully used
for production of starch-based biodegradable films.
INFERENCES
• Production of yeast-free continuous baked products can be
done using SCFX
• Fortification of heat labile micronutrient into extrudates
• Utilization of agro-food industry wastes into nutritionally
attractive by-products
• Biodegradable material can be produced using SCFX
CONCLUSION
• Development of dairy based extrudates using
SCFX
• Development of several biodegradable material
using SCFX
• Development of meat extrudates using SCFX
video
FUTURE THRUSTS
Supercritical fluid extrusion

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Supercritical fluid extrusion

  • 1. SUPERCRITICAL FLUID EXTRUSION (SCFX) PRAGATI SINGHAM Roll No.- 10703 Ph.D 1st year
  • 3. INTRODUCTION High temperature High shear Steam puffing Extrusion Technology Disadvantages
  • 4. High solubilizing capacity High Diffusivity Low temperature process Supercritical Fluid CO2 Advantages
  • 5. Supercritical Fluid Extrusion SUPERCRITICAL FLUID EXTRUSION (SCFX) Versatile High production Rate Low temperature Low shear High expansion
  • 6. SUPERCRITICAL FLUID EXTRUSION PROCESS (SCFX) • Development of gas holding rheological properties Injection of CO2 Nucleation of Cells Expansion
  • 7.
  • 8. OBJECTIVE To develop novel extrusion protocols to directly incorporating fruit/dairy by-products into shelf-stable, puffed, extruded products and evaluate changes in their quality due to processing.
  • 9. MATERIALS AND METHODS Materials Pre-gelatinized starch 76% Apple pomace powder (22% & 28%) Lecithin 1% Distilled monoglycerides, 1% At 7.58 MPa
  • 12.  Direct utilization of apple pomace into nutrient-enriched, shelf stable puffed extruded products  Retention of 84% of the Total Phenolic Content (TPC) and 74% of the total antioxidants  Low density extrudates 0.21-0.35 g/cm3 were obtained INFERENCES
  • 13. OBJECTIVE To produce soy based expanded crisps fortified with micronutrients and protein by using SCFX
  • 14. MATERIAL AND METHODS Lecithin (1.5g/100g), Distilled monoglycerides (1g/100g), Table Salt (1.5g/100g) Micronutrient premix 325mg/100g Flour % Soy protein Conc. (RS SPC-25) % Soy protein Conc. (RS SPC-40) % Soy flour (RS SF-25) % Soy flour (RS SF-40) Waxy rice flour (WRF) (g/100g) 71.5 56.5 71.5 56.5 Rice-Soy Concentrate Crisps (A) 25% (B) 40% Rice-Soy Flour Crisps (A) 25% (B) 40%
  • 15. 0 0.1 0.2 0.3 RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40 RSC-SPC 25 RSC-SPC 40 RSC-SPC 40 RSC-SF 40 Piece Density (g/cm3) Bulk Density (g/cm3) 0 1 2 3 4 5 RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40 Expansion Ratio (%) Density Expansion Ratio RESULTS
  • 16. -0.6 -0.4 -0.2 0 0.2 0.4 0.6 0.8 RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40 a value 59 60 61 62 63 64 RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40 L value 0 4 8 12 16 RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40 b value COLOR
  • 17. 0 2000 4000 6000 8000 10000 12000 RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40 Vitamin A (IU/100g) Before Extrusion After Extrusion 0 20 40 60 80 100 120 140 160 RSC-SPC 25 RSC-SF 25 RSC-SPC 40 RSC-SF 40 Vitamin C (mg/100g) Before Extrusion After Extrusion MICRONUTRIENTS
  • 18. RSC-SPC 25 was found to be best among the samples Improved amino acid balance due to incorporation of soy protein to rice flour No undesirable quality attributes on fortification of vitamin A, C and minerals. Effective process based nutrient fortification approach to reduce malnutrition. INFERENCES
  • 19. OBJECTIVE To quantify the effects of die temperature, different levels of alkalized cocoa powder and CO2 gas injection on cellular structure and physical properties of extruded meal
  • 20. MATERIAL AND METHODS Corn meal Variables Temperature 95˚C, 110 ˚C and 120˚C Alkalized cocoa powder (6% and 12%)
  • 21. RESULTSSectionalExpansionIndex(SEI) Effect of die temperature, ACP content and C02 gas injection EXPANSION INDEX PIECE DENSITY
  • 22. 0% 6% 12% ACP 95˚C 110˚C 120˚C 95˚C 110˚C 120˚C DIE TEMPERTURE CELL STRUCTURE Without CO2 injection With CO2 injection
  • 23. Die temperature, Alkalized Cocoa powder (ACP) content and CO2 injection significantly affected the physical properties of the extrudates Addition of ACP imparted rigidity to the extruded structure and reduced shrinkage Uniform microcellular structure with reduced breaking strength in ACP added CO2 injection process INFERENCES
  • 24. OBJECTIVE To develop SCFX leavened dough and breads with density comparable to the density of conventionally yeast-leavened breads and commercial bread products
  • 25. MATERIAL AND METHODS Dough Formulae Percentage Flour Weight Ingredients Formula 1 Formula 2 Formula 3 Guar Gum 0.5 0.15 Nil Egg powder 1 0.5 Nil Ascorbic acid 0.01 0.2 0.2 Conventional baking 180˚C for 30 min Combined Vacuum and Conventional 188 ˚C with 50.8kPa vacuum for 30 min followed by 180 ˚C for 10 min.39 rpm
  • 27. 0 0.1 0.2 0.3 0.4 0.5 C V+C C V+C C V+C Formula 1 Formula 2 Formula 3 Bread Density (g/cm3) 0 10 20 30 40 C V+C C V+C C V+C Formula 1 Formula 2 Formula 3 Crumb Moisture (%) PHYSICO-CHEMICAL PROPERTIES
  • 28. FORMULA 2 STALING TEST Conventional Baking Combined Conventional and vacuum baking
  • 29. Formula 2 yeast-free bread produced by combined conventional vacuum baking using SCFX leavened dough was found to be the best Density and crumb hardness obtained in SCFX leavened bread was comparable to yeast leavened breads Bread quality was controllable as compared to conventional yeast-leavened bread Consistent ready-to-bake dough can be produced in shorter time (approx. 0.36 to 0.41 h ) without ethanol emmission INFERENCES
  • 30. OBJECTIVE To study the cross-linking of native/pre-gelatinized starch blends and to create cross-linked microcellular starch foams by reaction SCFX with STMP
  • 31. MATERIAL AND METHODS Samples: Pre-gelatized wheat starch Control mixture of native starch (40% w/w)and pre-gelatinized starch (60% w/w) Food-grade Sodium Trimetaphosphate (STMP): 9% NaOH (0.1 M, 0.2 M) SC-CO2: 0%, 1% and 1.5%
  • 32. DENSITY and EXPANSION RATIO RESULTS
  • 34. 0 5 10 15 20 25 30 0% 1% 1.50% SC-CO2 (% DRY FEED) 9% STMP 0.1 M NaOH at 60˚C 9% STMP , 0.1 M NaOH at 90˚C 0 2 4 6 8 10 12 0% 1% 1.50% SC-CO2 (% DRY FEED) 9% STMP 0.2 M NaOH at 60˚C 9% STMP , 0.2 M NaOH at 90˚C WATER SOLUBILITY
  • 35. Cross-linking, modified and integrated the structure of extrudates High pH, low temperature favoured restricted mobility which leads to decrease in water solubility pH played a key role in reactive supercritical fluid extrusion Reactive Supercritical fluid extrusion can be successfully used for production of starch-based biodegradable films. INFERENCES
  • 36. • Production of yeast-free continuous baked products can be done using SCFX • Fortification of heat labile micronutrient into extrudates • Utilization of agro-food industry wastes into nutritionally attractive by-products • Biodegradable material can be produced using SCFX CONCLUSION
  • 37. • Development of dairy based extrudates using SCFX • Development of several biodegradable material using SCFX • Development of meat extrudates using SCFX video FUTURE THRUSTS

Editor's Notes

  1. DM –conditioner, anti scticking and stablizing agent Lecithin emulsifier evn mixing improve text n mouthfeel]table salt flavour enhancer
  2. Non strach binds the water , hardness
  3. Guar gum moisture inc and egg powder Density reduce by 25-36%