simulation of industrial frying of potato

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Azmil Haizam Ahmad Tarmizi and Razali Ismail Malaysian Palm Oil Board Lembaga Minyak Sawit Malaysia Simulation of industrial frying of potato chips using a pilot plant continuous fryer: Physico-chemical changes in palm olein binary blends under continuous frying conditions

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Azmil Haizam Ahmad Tarmizi and Razali Ismail Malaysian Palm Oil Board

Lembaga Minyak Sawit Malaysia

Simulation of industrial frying of potato

chips using a pilot plant continuous

fryer: Physico-chemical changes in

palm olein binary blends under

continuous frying conditions

Background of frying

Study case

Design of experiment

Research outcomes

Conclusions

Take home message

Presentation outline

More than 20 million tonnes of edible oil

production is used in frying sectors (Dana and

Saguy, 2006; Gertz, 2004)

Frying is a dehydration process that involves

immersion of food in hot oil when food is heated

above water saturation temperature (Farkas and

others 1996)

Simplicity in frying operation, convenience and

economic viability resulted in extensive sales of

fried food

Frying process

Heat transfer media

Remove water

Unique sensory properties

Impart of fried food

Provide high energy

Modify food texture

Make food palatable

Source of vitamins

Essential fatty acids

Acts as lubricant

Roles of frying

Potato chips

30 – 40%

Tortilla chips

22 – 26%

Frozen French fries

4 – 7%

French fries

12 – 15%

Breaded products

13 – 20%

Battered products

14 – 17%

Instant noodles

18 – 21%

Doughnuts

22 – 26%

How much oil in your favourite snacks?

“...As significant amount of frying

oil is becoming part of the fried

food, oil quality and stability is of

major concern to consumers...”

Naturally stable oils

Breeding

Hydrogenation

Blending

Additives

How to improve oil stability?

Stability of palm olein has extensively

discussed on batch or intermittent frying,

however, limited for continuous frying

The prospect of palm olein for frying

seems to be denied by:

1. misleading perception associated to

saturation level; and

2. strong preference to local oils

Palm olein is known as a heavy duty frying due to its techno-

economic advantages over other oils

Palm olein for industrial frying

Objectives

• To study the stability of palm

olein when blending with (a)

sunflower oil; (b) canola; and (c)

cottonseed oil, respectively;

• To compare (a), (b) and (c) with

that of palm olein as reference

oil (control);

• To investigate the stability of

potato chips up to 4 months of

storage

Expected benefits

• Expose food processors on the

benefits of blending soft oils with

palm olein for industrial frying;

• Increase the market share of

palm olein in countries or regions

that have strong preference to

their locally produced oils

Therefore…

Preparation and experiment setup

Variables Conditions

Fryer capacity 200 L

Frying temperature 180 ± 2 oC

Frying time 2 min

Oil turnover time 8 h

Production 50 kg h-1

Total frying time 40 h (8 h daily for 7 days)

Frying interval Continuous

Oil replenishment Continuous

Filtration Continuous

Oil sampling Interval of 2 h

Product sampling Mid-day daily

Raw materials

Palm olein (PO)

Sunflower oil (SFO)

Canola oil (CNO)

Cottonseed oil (CSO)

Atlantic variety potatoes

Oil blends

60% PO + 40% SFO

70% PO + 30% CNO

50% PO + 50% CSO

Continuous

fryer

Conditioner

Control

panel

Used and fresh oil tanks

Packaging room

Slicer

Air dryer

Pilot plant continuous fryer

Loading Peeling Sorting Slicing and conditioning

Air-drying FRYING Flavouring Packaging

1 2 3 4

5 6 7 8

Frying operation

Analyses

Frying oil

Fatty acid composition

Iodine value

Tocols

Induction period

Colour

Free fatty acids

Smoke point

Peroxide value

p-Anisidine value

Total oxidation

Polar compounds

Polymer compounds

Product

Shelf-life stability

Sensory evaluation

Research outcomes…

Fatty acid composition A

fter

ble

nd

ing

B

efo

re b

len

din

g

C18:3 = 6.20%

C18:3 = 2.14%

Parameter PO SFO CNO CSO PO + SFO PO + CNO PO + CSO

C18:2 / C16:0 0.27 8.76 4.63 2.37 1.16 0.48 1.02

Polyene index 0.25 5.53 3.72 2.05 0.99 0.49 0.89

Iodine value (Wijs) 56.21 112.79 108.65 110.71 85.53 71.68 82.60

Tocols

Frying time (h) Tocols (mg kg -1)

PO PO + SFO PO + CNO PO + CSO

0 587 ± 17 546 ± 15 497 ± 29 523 ± 16

8 475 ± 23 497 ± 5 397 ± 35 461 ± 22

16 393 ± 32 418 ± 11 318 ± 26 484 ± 20

24 414 ± 28 402 ± 9 333 ± 30 378 ± 17

32 394 ± 17 374 ± 19 276 ± 24 323 ± 19

40 401 ± 20 392 ± 18 395 ± 47 305 ± 24

48 393 ± 30 383 ± 18 267 ± 19 352 ± 31

56 379 ± 32 374 ± 15 278 ± 17 327 ± 18

Induction period

Frying time (h) Induction period (h at 110 o C)

PO PO + SFO PO + CNO PO + CSO

0 21.4 ± 1.5 10.6 ± 0.2 11.3 ± 0.9 8.3 ± 0.5

8 15.3 ± 1.0 9.2 ± 0.5 9.1 ± 1.0 7.0 ± 0.3

16 16.1 ± 0.7 8.9 ± 0.2 7.8 ± 0.8 7.5 ± 0.5

24 14.6 ± 0.7 8.9 ± 0.3 5.9 ± 0.5 6.1 ± 0.5

32 15.2 ± 0.6 9.0 ± 0.5 6.2 ± 0.7 4.0 ± 0.4

40 14.6 ± 0.7 8.6 ± 0.2 5.3 ± 0.5 4.3 ± 0.5

48 15.2 ± 0.9 8.7 ± 0.3 5.7 ± 0.6 3.7 ± 0.6

56 14.8 ± 1.1 8.6 ± 0.3 4.9 ± 0.9 3.9 ± 0.5

Colour

Frying time (h) Colour (Redness)

PO PO + SFO PO + CNO PO + CSO

0 2.8 ± 0.2 1.4 ± 0.1 1.2 ± 0.1 2.4 ± 0.3

8 8.3 ± 0.5 4.1 ± 0.1 4.8 ± 0.3 5.2 ± 0.5

16 10.6 ± 0.7 5.1 ± 0.2 8.6 ± 0.4 9.0 ± 0.4

24 11.7 ± 1.1 6.4 ± 0.4 10.3 ± 0.7 11.0 ± 0.1

32 15.5 ± 0.6 6.6 ± 0.3 11.9 ± 0.1 12.6 ± 0.4

40 18.1 ± 0.9 7.2 ± 0.1 12.4 ± 0.4 12.1 ± 0.1

48 19.3 ± 0.5 8.3 ± 0.3 12.0 ± 0.1 12.5 ± 0.5

56 21.2 ± 0.5 9.5 ± 0.3 13.2 ± 0.4 12.8 ± 0.1

Free fatty acid

Smoke point

Total oxidation

Frying time (h) Total oxidation (unit)

PO PO + SFO PO + CNO PO + CSO

0 2.2 ± 0.8 4.2 ± 0.5 8.2 ± 0.7 6.5 ± 0.8

8 33.7 ± 2.5 28.5 ± 1.4 37.7 ± 2.3 33.2 ± 1.6

16 40.8 ± 2.3 40.1 ± 2.3 45.1 ± 1.7 34.7 ± 3.5

24 42.0 ± 4.1 35.5 ± 2.6 55.4 ± 3.7 52.8 ± 4.2

32 43.4 ± 3.0 38.9 ± 2.1 64.5 ± 3.4 65.0 ± 2.9

40 38.5 ± 1.9 42.3 ± 3.5 68.3 ± 5.0 54.1 ± 3.9

48 37.3 ± 4.1 35.9 ± 2.1 63.3 ± 4.4 58.5 ± 3.9

56 40.7 ± 3.9 41.1 ± 2.9 70.9 ± 2.6 63.9 ± 0.5

Polar compounds

Polymer compounds

Shelf life stability and sensory evaluation

In general, the binary mixtures of palm olein with sunflower, canola

and cottonseed oils resulted in comparable oil stability with that of

palm olein under continuous frying conditions

Stability of the oil blends also reflected by acceptable sensory

properties of potato chips even after 4 months of storage

Data generated provides useful information on stable frying oils

without the need to fully replace their local oils

Conclusions

The cost of frying operation is lowered whilst the shelf life of oil is

relatively improved

For more information…

Ahmad Tarmizi AH, Ismail R. 2014. Use of pilot plant scale continuous

fryer to simulate industrial production of potato chips: Thermal

properties of palm olein blends under continuous frying conditions.

Food Sci Nutr (In press).

Ahmad Tarmizi AH, Ismail R. 2008. Comparison

of the frying stability of standard palm olein and

special quality palm olein. J Am Oil Chem Soc

85(3):245-251.