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Sidal Acun

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Filter's pore size: customize the retentate and permeate ... Recirculating permeate at high speed in the same direction as the retentate with ... – PowerPoint PPT presentation

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Title: Sidal Acun


1
MICROFILTRATION APPLICATIONS IN DAIRY INDUSTRY
  • Sidal Acun
  • Yrd. Doç. Dr. MERAL KILIÇ

2
Microfiltration
  • Sieving process
  • The most open or porous in the filtration
    spectrum.

3
Microfiltration
  • Non-thermal or less thermal improves milk
    quality
  • Retentate pore diameter gt membrane pore diameter
  • Permeate pore diameter lt membrane pore diameter
    (also named microfiltrate)

4
Microfiltration
  • Separation of small particles about 0.1 to 10 µm
    size range with operating pressures of 0.050.2
    MPa.

5
Microfiltration
  • Cross-filtration flow parallel to the membrane
    surface, also named cross flow microfiltration

Cross flow microfiltration
6
Microfiltration
  • Ceramic membranes strong mechanical resistance
    and wide tolerance to pH (0.3 to 13.5).
  • Monotubular and multichannel monoliths

7
Ceramic Membrane Element
8
Microfiltration
  • Pore size bubble point method
  • Filters pore size customize the retentate and
    permeate
  • Liquid flux Retention of particles or bacteria
    of certain sizes.

9
Microfiltration Applications
  • Main applications
  • Removal of bacteria and spores
  • Fat seperation (especially for whey)
  • Micellar casein enrichment of the cheesemaking
  • Milk protein fractionation

10
Removal of Bacteria and Spores
  • Reduce the microbial load of raw milk
  • 20.000 CFU m/L skim milk - microfiltration - lt
    10 CFU m/L skim milk
  • Microfiltration 100 C 2 s Shelf life ranging
    from 6 to 9 months.
  • Sensory tests show much beter than UHT milks.

11
Removal of enzymes
  • if heating effectively kills most of the
    microbial flora, the dead cells remain in the
    milk with their potentially active enzymes that
    with the metabolic activity developed by the
    growth of the remaining thermoduric bacteria,
    will cause alterations of liquid milks during
    storage, thus reducing shelf-life

12
Fat Seperation
  • Whey defatting seperation of aggregated calcium
    phospolipid complex by MF (0.1 µ m pore size).
  • Fractionation of globular milk fat (SG and LG)
    drinking milk, yoghourt, sour cream, butter,
    camembert cheese, fresh cheese.
  • E.g. skim milkreference cream (1) MF permeate
    (SG) from raw milk (2)
  • Same fat content (17 g.kg-1) 2 is more creamy
    than 1

13
Casein enrichment
  • Casein enrichment (10 µ m MF) pizza cheese,
    coffee whitener
  • Micellar casein enrichment (0.1 µ m) improve
    quality of cheese (camembert)and increase
    capacity of cheese plant.

14
Casein enrichment
  • Gelation Study
  • Skim milk 4 C MF, 0.2 mm, 0.1 mm, or 100 000
    g.mol-1 MWCO
  • Permeate 10 000 g.mol-1 MWCO 9 solids
    retentate
  • Reduced the caseinwhey protein ratio and
    increased
  • the b-caseina-casein ratio
  • Formed softer gels that had greater syneresis and
    hydration,
  • and lower water holding capacities than skim milk
    gels.

15
New-dairy based powder
  • Mozarelle cheese
  • Combination of MF (0.1 and 0.2 mm) and UF
  • Avoid b-lactoglobulin-k-casein complex during
    thermal processing
  • Rennet coagulability, melting properties and
    improvements
  • Cheesemaking yields were 7.3 1.8 higher (with
    milk powder) in comparison with the control
    cheese (with raw milk)

16
Milk protein fractionation
  • a-lactalbumin-enrichment for infant formulas
  • Ceramic membrane 0.1 µ m
  • Process 1. step thermal treatment b -LG
    denaturation (a-LA/b -LG 0.3 to 4)
  • 2. step a-LA Microfiltration
  • Skim milk microfiltration- low heat milk
    powder, milk proteins concentrates or micellar
    casein powder.

17
Transmembrane Pressure
  • Membrane inlet pressure cause fouling
  • Increasing shear rate dont help
  • Recirculating permeate at high speed in the same
    direction as the retentate with same axial
    pressure Uniform Trans-Membrane Process Pressure
    (UTP)

18
Conventional UTP
19
Disadvantage Fouling
  • Concentration of fluid, flow rate, TMP, type of
    membrane material, pore size
  • Decrease filtration efficiency
  • Native proteins start transforming into denatured
    and aggregated proteins
  • Distilled with rinsing wateralkaline solution
  • a-Lactalbumin fouling

20
Disadvantage Expensive
  • Cheese brine purification
  • MF in a UTP equipment with a pore size of 1.4 µ m
    or 0.8 µ m
  • UTP expensive investment cost

21
  • The manufacturing cost of MF Cheddar was slightly
    higher than the manufacturing cost of
    conventional Cheddar.
  • However, the benefit in net revenue from the use
    of MF was estimated to be higher than the
    difference in manufacturing costs.

22
Advantages
  • Hygienic safety with minimal heat treatment
  • Keeping nutritional and bioactive properties of
    milk components
  • Dairy research development without any bias
    (önyargi)
  • Efficient cheese-making
  • New milk derivatives milk protein and fat
    fractionation

23
Microfiltration-Pilot Plants
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