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Current and Emerging Processing Technologies for Seabuckt horn (H i ppopha erhamnoides  L.) and Its Products  Alphonsus Utioh, P. Eng. Manager, Product and Process Development Food Development Centre  A Member of Manitoba Agri-Health Network Presented at ISA 2007 Conference, Quebec City, Canada  August 12–16, 2007 

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Current and Emerging Processing Technologies for

Seabuckthorn (Hippophae rhamno ides L.) and Its

Products

 Alphonsus Utioh, P. Eng.

Manager, Product and Process Development

Food Development Centre

 A Member of Manitoba Agri-Health Network

Presented at ISA 2007 Conference, Quebec City, Canada August 12–16, 2007 

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Presentation Outline

• Introduction – FDC and MAHRN• Harvesting Technologies

• Seabuckthorn (SBT) –  A Plant with Many Uses

• Processing Technologies

 – Juice Processing – Oil Processing

 – Leaf Processing

• Summary

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Food Development CentreServices and Capabilities

• A Special Operating Agency ofManitoba Agriculture, Food andRural Initiatives (MAFRI)

• A member of Manitoba Agri-Health Research Network(MAHRN)

• Engine of economic developmentfor Manitoba and the agri-food

industry

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Service Lines

• Product Development Services

• Process Engineering Services

• Pilot Plant Commercial Processing

• Analytical Support Services

• Library and Information Services

• Training

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Harvesting Technologies

• SBT has bright yellow or orangefruits

• Manual• Hand-picking

• Using metal hooks

• Manual harvesting is labour intensive and expensive butproduces very clean fruits forprocessing

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Harvesting Technologies

• Shrub Shaking

 – Limited success reported on Indian

Summer variety

 – Damage to tree trunks reported

• Cut-and-Freeze/Cut-and-Harvest

 – Most effective and economicalmethod for a wide range of SBT

varieties

 – Limits production due to alternating

harvest

Kranemann Gartenbaumaschinen GmbH

Reproduced with permission

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Seabuckthorn – a plant with many uses

Plant Part Component UsesFruits Pulp, seed, juice Food, drinks,

pharmaceuticals

Pulp Oil Pharmaceuticals,cosmetics, pigment

Seeds Oil Pharmaceuticals,

cosmetics

Leaves Sterols, Flavonoids, Pharmaceuticals,

carotenoids cosmetics, teas

Bark Hippophan (5-hydroxytryptamine), Pharmaceuticals

proanthocyanidins

Roots Soil conservation,land reclamation

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Chemical Components of Seabuckthorn

• Fruits contain

 – Many bioactives includingvitamin C, vitamin E,

flavonoids and

carotenoids• Seed and Pulp Oils

 – Known for their fat-

soluble vitamins, plantsterols, essential fatty

acids

Ferme Nicole

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What Makes SBT Fruit Unique

0.18-0.2 mg (250 g of

fruit)Up to 0.08 mgFolic acid

8-10 mg (5 g of oil)Up to 200 mg

(300 IU)Vitamin E

60 mg (< 10 g of fruit)

500-1,000 mg

(700 mg)Vitamin C

Recommended Daily

Intake (RDI)

 Amount

(per 100 g offruit or oil)

Constituent

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What Makes SBT Fruit Unique

3.5-4.4 (%

malic)

Organic acids (malic and quinic major

ones)

100-1000

mg/100g of

fruits

Flavonoids (e.g., mainly isorhamnetin,

quercetin glycosides, and kaempferol

30-40 mg/100g

of fruits

Carotenoids, including β-carotene,

lycopene, zeaxanthin

6-11%Unsaturated: oleic acid (ω-9), palmitoleicacid (ω-7), palmitic acid and linoleic acid

(ω-6), and linolenic acid (ω-3)

Saturated and sterols (mainly β-

sitosterol)

 AmountConstituent

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Seabuckthorn Processing

 

Fruit

Centrifugation

Puree

Separation

Pulp/Finisher

Seed

Dried pulp

- Nutritional bar- Pulp oil- Pigment, etc.

Clarified juice

Seed oil

- Juice- Beverage- Jelly- Wine, etc.Oil extraction

Skin and seeds

Drying Paste

SEABUCKTHORN 

Air/Freeze drying

Dried fruits

Spray drying

Juice powder

Leaf

Air/Freeze drying

Grinding

SBT tea

Extraction

Bio-actives

Bark

Bio-actives

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SBT Juice Processing

• Fruit selection/cleaning

 – Important to remove stems,leaves and other debris

 – Ideally should be doneduring harvest before

storage

• Pressing

 – Making sure all the fruits

break to release juiceduring pressing

 – Pulper/Finisher isrecommended

Pulper/Finisher 

Belt Press Juice Extractor 

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SBT Juice Extraction

S b kth J i E t ti C td

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Seabuckthorn Juice Extraction Contd.

• Juice Clarification

 – Fresh juice extracted canseparate into three phases

if not clarified:

• an upper cream phase,• juice in the middle, and

• a sediment at the bottom

 – In some jurisdiction pulpy

 juice is accepted by

consumers

Unclarified Juice

Cream

Phase

Sediment

Phase

Liquid

Phase

SBT J i E t ti C td

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SBT Juice Extraction Contd.

• Juice Clarification

 – High speed centrifuge ofthe disk stack type isrequired for separation

 – Sediment is removedfrom the bottom of thebowl by de-sludgingmechanism

 – Homogenization of the juice could remove anyoil layer on the juicesurface

Clarified Juice

Disk Stack Separator 

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Other Technologies in Juice Processing

• Enzymatic Hydrolysis

 – Use of commercial proteolytic,pectinolytic and cellulytic enzymesduring juice extraction:

• To improve juice release from the tissue

• To reduce juice viscosity and

• To improve separation of suspendedsolids by centrifugation, sedimentation orfiltration

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Other Technologies in Juice Processing

• Membrane Filtration

 – The separation of components of a liquid or fluid using a

thin barrier or film of material (membrane filter) through

which fluids and solutes are selectively transported when a

driving force is applied

 – Membranes can be made of organic polymers or inorganic

materials such as ceramics

Retentate

Permeate

FeedMembrane

Recycle

Membrane Filtration Schematic

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Membrane Separation Categories

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Membrane Separation Categories

S C

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Membrane Separation Categories

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SBT Juice Extraction Contd.

Juice Pasteurization

Methods: – High-temperature-short-time

(HTST) at 80-90oC

 – UHT Aseptic Processing

• HTST SBT juice could turn

brown if stored for more than 6

months at 15-20o

C• Storage under at 2-4

oC

prolongs the shelf-lifeTetra Therm Aseptic Pilot

System

S D i P f SBT J i

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Spray Drying Process for SBT Juice

Concentrate

Cyclone

 Air 

Tank

Pump

Exhaust

 Air 

Coarse Powder 

Fine Powder 

Filter 

Fan

Heater 

Spray Nozzle

Compressed

 Air 

T i l Ch t i ti f SBT J i

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Typical Characteristics of SBT Juice

Component Characteristic/ContentColour Yellow

Yield 57 - 75%

Soluble solids 9.3 – 15.5o

BrixpH 2.7-3.13

Vitamin C 150-709 mg/100mL

Organic acid (% malic) 3.5 - 4.4

Potassium 100-806 mg/mL

Sodium 17.7-89.8 mg/mL

Zinc 0.43-6.31 mg/mL

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Seabuckthorn Juice Products

Samples of Christine Berger Gmbh ProductsJuice JamLiquor Wine

SBT Juice Powder 

Produced at FDCSBT Beverages in Tetra Pak

Seabuckthorn Indage Ltd. India

SBT Juice

Sibu International

SBT Oil E t ti

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SBT Oil Extraction

Extraction Technologies:• Cold Press

• Solvent Extraction

• Supercritical Fluid Extraction• Friolex Process

• Enzymatic Process

• Microwave Assisted ProcessSBT Seeds

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SBT Oil Extraction Contd.

• Cold Press Process – Expellers have rotating

screw inside a horizontalcylinder 

 – Screw forces the seeds

through the cylindergradually increasing thepressure

 – Oil escapes from the cylinder

through small perforations

 – Temperature and pressurecan be adjusted for efficientextraction and oil quality

 – Material preparation isimportant

Motor Feeding Hopper  

Press Cylinder 

PressHead

Screw Press

Oil Outlets

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Solvent Extraction of Vegetable Oil

Condensation

B Y P R O D U C T

Precipitation

Oilseed

SaladOil

© R.D. Reichert 2000

Degumming& Deacidification

Decolorization

Deodorization

Hexane Extraction

Gum

Deodorizer Distillate

Crude Vegetable OilPressed

Oil

Pressing

CookingOil

Winterization

 

C l a s s

P h o s p h a t id e s

S t e r o l in s

F r e e F a t t y A c i d s

C a r o t e n o i d s /C h l o r o p h y l l s

S t e r o l s

T o c o p h e r o l s

T o c o t r i e n o l s

S O C

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SBT Oil Extraction Contd.

Supercritical Fluid Extraction• Unique separation process

• Uses properties of gas or liquidabove its critical temperature andpressure for extraction:

 – high density for good solventpower 

 – low viscosity and diffusivity

for appreciable penetratingpower 

• Commonly used gas is carbondioxide

Phase Diagram

SBT Oil Extraction Contd

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SBT Oil Extraction Contd

CO2

Supercritical Fluid Extraction Process

Oilseed/Pulp

Cleaning

Crushing/Flaking

Extraction

Oil separation

SBT Oil

SBT Oil Extraction Contd

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SBT Oil Extraction Contd.

Friolex Process – Patented

• Centrifugal technology for oilrecovery

• Water-based oil extraction process

• Uses alcohol as a processing aidto break down the emulsion

• A special decanter centrifuge forseparating the oil from the meal

• Oil impurities are removed in ahigh speed separator 

• Process is blanketed with an inertgas (nitrogen) for product quality

Phase Diagram

Westfalia Decanter CentrifugeReproduced with permission

Friolex Process

SBT Oil Extraction Contd

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SBT Oil Extraction Contd

Drying

Slurry

 Alcohol

Water 

Reproduced from Westphalia Separation

Industry Brochure

Friolex Process Oilseed/Pulp

Cleaning

Crushing/Flaking

Mixing

Oil separation

Oil drying

SBT Oil

SBT Oil E t ti C td

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SBT Oil Extraction Contd.

Microwave-Assisted Extraction

• Based on selective and localizedheating of moisture in the

material by microwaves

• Pressure builds up within the

tissue leading to rapid masstransfer of the oil into the solvent

• The slurry is separated and the

oil is purified

• The carrier solvent is selected so

as to be transparent to

microwaves – only the oilseed

mass is heated.

Microwave-Assisted Oil Extraction

S b kth Oil

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Seabuckthorn Oil

Supercritical Omega 7

S b kth P d t

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Seabuckthorn Products

Topical cream

Encapsulated SBT oil extract

Seabuckthorn lip balm

SBT Leaves

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SBT Leaves

• SBT leaves contain nutrients andbioactives such as :

 – Carotenoids, sterols, flavoniods, fatty acids,

minerals, vitamins and other phytochemicals

 – Can be processed into herbal teas, andextracts for pharmaceutical and cosmeticapplications

Drying of SBT Leaves

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Drying of SBT Leaves

• Two Basic Technologies:

 – Convection Air Drying• Most basic yet effective and commonly

used in the industry

• Equipment such as a tray dryer e,g.Proctor and Schwartz Dryer 

Tray Dryer 

Typical SBT Leaf Drying Results

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Typical SBT Leaf Drying Results

Drying time (min)

0 50 100 150 200 250

   M  o   i  s

   t  u  r  e  c  o  n   t  e  n   t   (   %   w

   b   )

0

20

40

60

80

50

o

C60oC

80oC

100oC

870 d 610.8 0.3100

838 d 1392.2 0.580

1123 b 23.62.2 0.560

1042 bc  77.52.8 0.750

1453 a 15375.5 1.2Fresh leaves

Total Phenolics

(mg/100 g wb)

Equilibrium

Moisture (%)

Drying

Temperature (ºC)

Total phenolics of fresh sea buckthorn leaves and

leaves dried to the equilibrium moisture content of

50, 60, 80 and 100 ºC.

Moisture changes of sea buckthorn

leaves during

convection drying at 50, 60, 80 and

100 ºC.

Stefan Cenkowski, et al. J. of Food Science, Vol.70, No. 9, 2005 reproduced with permission

Drying of SBT Leaves Contd

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Drying of SBT Leaves Contd.

• Freeze Drying – Freeze drying, or lyophilization, is the process of

removing water from a product by sublimation.

 – Freeze drying is an attractive option for drying of heat

sensitive high-value products.

Freeze Dryer at

FDC

Equipment consist of:

-drying chamber with shelves

-Condenser to trap removed

moisture

-Cooling system to supply

refrigerant

-Vacuum system to facilitate

drying

SBT Tea Product

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SBT Tea Product

Tea Bar 

Tea Soap

Tea Leaves

Summary

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Summary

• Processing technologies, both current and

emerging, have significant impact on the quality ofseabuckthorn products

• It is important to evaluate the market potential ofthe products associated with each technology

before implementation

• More research is required on processing

technologies in order to maximize the quality and

yield of seabuckthorn products

Acknowledgements

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 Acknowledgements

• Canada-Manitoba Agri-Food Research

Development Initiatives (ARDI) for providing fundingfor SBT Research Program

• Branching-Out Orchards and Mrs. Angela Dueck forproviding SBT fruits for our research program

• FDC staff especially: Dr. Haihong Wang, Dr. Paulyn

 Appah, and Ms. Janice Meseyton for managing SBT

research program at FDC

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Thank you