Title: Flow and Filtration: The Physics of Brewing
1Flow and Filtration The Physics of Brewing
- Dr. Alex Speers
- Department of Food Science and Technology
- ltAlex.Speers_at_dal.cagt
2Outline
- Introduction
- Brewing gums
- shearing
- Methods
- Rheometry
- Filtration
- Summary
3Why study ?-glucans?
- Cause processing problems in brewing
- Under-modification of barley endosperm
- High viscosity of wort and beer
- Slow runoff of wort and beer
- Haze formation in packaged beer
- Clogging of membranes
- Increased production cost
4Localization of barley ?-glucans
Structure of a barley kernel
5Beta-Glucan and Arabinoxylan Content of Selected
Beers (ug / ml)
6Chemical structure of barley ?-glucans
Unbranched chains of ?-D-glucopyranose residues
O
O
O
O
O
O
?-(1?4)- linkage ?-(1?3)- linkage
7Chemical structure of arabinoxylans
8Localization of gums
- Deposited mainly in in endosperm cell walls
- Barley endosperm cell walls contain
- 20 arabinoxylans
- 70 ?-glucans
- Barley aleurone cell walls contain
- 65-67 arabinoxylans
- 26-29 ?-glucans
- Beta-glucan content
- barley 0.14 - 8.9
- wort/beer 12 - 940 mg/L
9Non-Fermentable Brewing Gums
- Defined as Non Starch Polysaccharides Gums - warm
water extractable - Tend to viscosify wort and beer
- Thus, add body/foam stability
- In the distant past - not a problem
- With advent of membrane filters, tight production
schedules lighter beer - Pose problems in some breweries some times
10Beta-Glucan fringed micelles
11Micelle-like Aggregation
12Methods
13Rheological Definitions
- Science of deformation and flow
- Three important terms are shear rate (?), shear
stress (?) and viscosity (?) - note different
symbols used.
?
V, F
h
??? V/h, ?? F/A ?????
14Calculation Example
- Shear rate if dV 1 cm/s and h 1 cm?
- Shear rate 1cm/s 1 cm 1 /s
- Shear rate units /s or s-1
- Shear stress if F 0.001 N and A 1 m2 ?
- Shear stress 0.001 N/ m2 1 mPa
- Viscosity 1 mPa s
15Shear stress/shear rate measurement rotational
- RPM -gt shear rate
- Torque -gt shear stress
- Viscosity shear stress/shear rate
16Rheometry
- Cone and plate and coaxial fixtures
17Shear stress/shear rate measurement pipe flow
- Flow rate -gt shear rate
- Pressure loss -gt shear stress
- Viscosity shear stress/shear rate
- Best suited for measuring Newtonian flow
behaviour.
18Rheometry
19Rheometry
20Viscosity Dependence
- Temperature h A e DE/RT
- Concentration (gums,oP, Etoh)
- Shear rate
- Shear history
21Shear effects
22Shear effects
23Non-Newtonian Flow
- Found at high gum concentrations
24Rheological Notes
- Normally viscosity properly defined as apparent
viscosity - mPa s ( cP), - Kinematic viscosity is apparent viscosity divided
by density (Stokes) - (Misleading terms in literature),
- 1 mPa s is 1 cP viscosity of water at 20oC,
- Apparent viscosty depends on density,
temperature, shear rate and shear history.
25Rheological Notes
- Intrinsic Viscosity h
- Based on extrapolated Specific viscosity (h/ h s
-1)/c -gt0 - Can be used to determine shape of polymer based
on molecular weight - h K M a
26Effect of Concentration
Determination of C with 327 kDa b-glucan in a
control buffer
27Early Results
- Using 327 kDa b-glucan at 50 g/L,
- ethanol (0-7), maltose (0-15) and
- pH (3.6-5.2)
- Viscosities were significantly
- different (Plt0.05).
28Variation of h and C of b-glucan solutions
Treatment pH maltose ethanol h C
() () (mL/g) (g/L)
High ethanol 4.1 0.5 6.0 464 6.47 Low
ethanol 4.1 0.5 4.0 812 2.72 Control 4.1
0.5 5.0 815 3.11 High maltose 4.1
0.8 5.0 806 2.13 Low maltose 4.1
0.1 5.0 862 3.05 Low pH 3.6 0.5
5.0 741 3.95 High pH 4.5 0.5 5.0 827 3.05
29Why Sporadic?
- Depends on crop year
- Stressed plant tends to more b-glucan (Kendall)
30Why Some Breweries?
- Depends plant equipment
- Depends on process
- Possibly due to differences in shearing of wort
beer
31Brewing Shear Rates?
- Turbulent or laminar?
- NRE ???V L/ ?
- ??? density, V velocity L diameter ?
viscosity - Average shear rate in turbulence
- ? (?/?)3 / ?1/4
- ? average power dissipation per unit mass
32Brewing Shear Rates?
- Turbulent or laminar?
- Turbulent flow cascades to laminar flow at small
distance scales
33Brewing Shear Rates
- Defined by Reynolds number of 2000-3000
- Note Re DVr/h
- Also note V is the average pipe velocity
- Generally get turbulent flow
34Brewing Shear Rates
- Shear in Kettle 8600 s-1
- (Speers et al. 2002)
- Shear in Fermenter 20-60 s-1
- (Speers Ritcey, 1995)
- Shear in Yeast brink tank lt15 s-1
- (Kawamura et al. 1999)
- Average shear rate in pipe flow
- High 915 s-1
- Mean 500 s -1
- Low 175 s -1
35Membrane filtration
- Theory developed in 30s
- Based on capillary plugging due to gradual
restriction in diameter - Surdarmana et al. 1996 Tech Quarterly
- t/V t/Vmax 1/Qinit
- Vmax maximum filtrate volume
- Qinit intial flow rate
36Membrane filtration
- Theory developed in 30s
- Based on capillary plugging due to gradual
restriction in diameter - Surdarmana et al. 1996 Tech Quarterly
- t/V t/Vmax 1/Qinit
- Vmax maximum filtrate volume
- Qinit intial flow rate
37Filtration Apparatus
38Example Sudarmana Transform
- Medium viscosity arabinoxlyan in model beer
39Relation of Intrinsic Viscosity and Filtration
- 1/Vmax a h for membrane test
- Filterability negatively correlated with h for
commercial (DE) filtration - Membrane filtration more suited for detection of
b-glucan problems
40Conclusions
- Ethanol, pH and maltose effect viscosity
- Shear strong effect on filtration
- Shear within brewery typically turbulent average
40-1250 s-1 - Sudarmana fit works (Tech. Quart 3363)
41Acknowledgments
- Students !
- NSERC
- Labatt Brewing RD
- NSDAM
- Westcan Malting
- Canada Malting
- Pfeuffer GmbH and Profamo Inc (Viscomat automated
capillary rheometer)