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Fermentation management A practical guide Chris Boulton University of Nottingham Relevance of fermentation Key stage in whole brewing process Major impact on:- – Beer flavour Total flavour compounds formed Consistency of flavour – Process efficiency Conversion of extract to ethanol – Process consistency Cycle time consistency Fermentation – the brewers perspective Controlled conversion of wort to green beer Control parameters Yeast strain Wort composition Pitching rate Wort oxygenation – Temperature Fermentation – the yeasts perspective The aim of yeast pitched into wort is to grow Beer is the spent growth medium

Boulton Fermentation talk · 2012-09-05 · Fermentation management A practical guide Chris Boulton University of Nottingham Relevance of fermentation • Key stage in whole brewing

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Fermentation management A practical guide

Chris Boulton University of Nottingham

Relevance of fermentation

•  Key stage in whole brewing process •  Major impact on:-

– Beer flavour •  Total flavour compounds formed •  Consistency of flavour

– Process efficiency •  Conversion of extract to ethanol

–  Process consistency •  Cycle time consistency

Fermentation – the brewer’s perspective

•  Controlled conversion of wort to green beer

•  Control parameters –  Yeast strain –  Wort composition –  Pitching rate –  Wort oxygenation –  Temperature

Fermentation – the yeast’s perspective

•  The aim of yeast pitched into wort is to grow

•  Beer is the spent growth medium

The art / science of fermentation management

•  Manage the activities of yeast –  Response of the genome to conditions the cells are

exposed to in brewing –  Must consider whole of yeast brewery cycle

•  Propagation •  Pitching •  Fermentation •  Cropping •  Storage

–  Vital to consider influence of real-world practice

Assumptions Providing the control parameters are regulated in a

precise manner fermentation will proceed in a predictable manner and provide a consistent product

Control of basic parameters

•  Current best practice systems for in-line oxygenation and pitching rate are adequate

– Use of thermal mass flow meters for wort oxygenation

– Use of Aber yeast capacitance meter for control of pitching rate

Aber Biomass Meter

Use of Aber system in practice

00.20.40.60.811.21.41.61.82

Std. deviation

(days)

1 3 5 7 9 11 13 15 17 19Month

New system commissioned

Data are means for 28 x 1600hl fermenters

Theory versus practice

•  Theory –  The majority of studies

which have elucidated the relationships between fermentation control parameters and the response of the yeast genome and phenotype performed at small scale

–  Use defined systems with good control of pitching rate, oxygenation regime and precise start point

Real world factors •  Very large batch sizes

(up to 10,000hl)

–  Very long fill times –  Several batches of wort –  Usually high gravity worts

•  When to pitch? •  When to oxygenate? •  How homogenous are

conditions in fv? •  When to crop?

Assumptions

•  Fermentation commences when filling is completed

•  Conditions are homogenous in primary fermentation

•  Yeast separates from green beer and crop forms at end of fermentation

•  Yeast separation can be encouraged by crash cooling

Example 1 – prolonged wort collection time

Effect of collection conditions on yeast growth

!  Ale fermentation !  1500hl, 22oC top temp. !  5 x 300hl brewlength !  Ca 19h total collection time !  All yeast pitched with first brewlength !  All brewlengths oxygenated

0

20

40

60

80

100

120

0 2 4 6 8 10 12 14 16 18

Time (h)

Oxy

gen

conc

. (%

sat

n.)

Start of wort collection and pitching

Completion of wort collection

Dissolved oxygen concentration during wort collection

0200400600800100012001400160018002000

0 2 4 6 8 10 12 14 16 18 20 22 24

Time (h)

Wo

rt v

ol.

(hl)

0

2

4

6

8

10

12

Cel

l co

un

t (m

illio

ns/

ml)

Start of wort collection Completion of wort collection

Yeast concentration during collection

10

20

30

40

50

60

0200400600800100012001400160018002000

0 2 4 6 8 10 12 14 16 18 20 22 24

Time (h)

Wo

rt v

ol.

(hl)

0

2

4

6

8

10

12

Cel

l co

un

t (m

illio

ns/

ml)

Start of wort collection Completion of wort collection

Wort vol.

Yeast concentration during collection

10

20

30

40

50

60

0200400600800100012001400160018002000

0 2 4 6 8 10 12 14 16 18 20 22 24

Time (h)

Wo

rt v

ol.

(hl)

0

2

4

6

8

10

12

Cel

l co

un

t (m

illio

ns/

ml)

Start of wort collection Completion of wort collection

Wort vol.

Predicted cell count

Yeast concentration during collection

10

20

30

40

50

60

0200400600800100012001400160018002000

0 2 4 6 8 10 12 14 16 18 20 22 24

Time (h)

Wor

t vol

. (hl

)

0

2

4

6

8

10

12

Cel

l cou

nt (m

illio

ns/m

l)

Start of wort collection Completion of wort collection

Wort vol.

Actual cell count

Predicted cell count

Yeast concentration during collection

10

20

30

40

50

60

Example 2 – When to pitch

Effect of multiple pitching

•  When to pitch? •  All with 1st brewlength or throughout

collection?

•  Example – 80% yeast pitched with 1st brewlength – 20% pitched with 4th of 5 brewengths

Yeast at completion of vessel fill

Yeast at completion of vessel fill

Yeast at completion of vessel fill

Example 3 – when to oxygenate

Roles of oxygen

Oxygen has dual roles as a yeast nutrient and a metabolic signalling molecule

–  Oxygen influences yeast growth extent

–  Oxygen influences beer volatiles •  Inhibits terminal ester forming enzyme, alcohol:acetyl

transferase (AAT) •  Represses ATF1 gene which codes for AAT

–  Timing of exposure of yeast to oxygen is as important as actual oxygen concentration

Early pitch Late pitch

Batches of oxygenated wort

1 2 3 4

Relationship between time of pitching and oxygenation

Late pitching provides same total oxygen concentration but reduces exposure time

Early pitching prolongs exposure time of yeast to oxygen

Effect of time of oxygen delivery on

ester formation

0

510

15

20

2530

35

40

0 50 100 150 200

Time (h)

Ethy

l ace

tate

(ppm

)

8hl Pilot scale fermentation

All oxygen delivered at pitch

Same total oxygen conc. delivered for

8h after pitching

Example 4 – fermenter heterogeneity

Assumptions

•  Convection currents ensure good mixing

•  Good mixing ensures homogeneity of temperature and yeast concentration

•  Yeast sedimentation is triggered by exhaustion of fermentable sugars and accelerated by application of cooling

Yeast distribution in fermenter is predictable

Experimental system •  Aber biomass meter

gives real time measure of viable yeast concentration (and temperature) as output

•  Probes in waterproofed enclosures have been immersed in a conical fermenter

Experimental system

Experimental system

Test Fermenter (1600 hl)

Multiplexer

Biomass Meter

Data output to networked PC

Biomass probes

Supporting stainless steel cable

Pivoted boom arm

Cable for lowering boom

Supporting frame and winch

Cable anchored to cone

Yeast concentration – top probe

!

"!

#!

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&!

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80

60

40

20

0

PG

Time (h)

Cel

l cou

nt (m

illio

ns/m

l)

1490 hl

Yeast concentration – middle cone probe

!

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#!

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%!

&!

'!

(!

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!

#!

%!

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300

200

100

0

PG

Time (h)

Cel

l cou

nt (m

illio

ns/m

l)

65 hl

!

"!

#!

$!

%!

&!

'!

(!

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!

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"!!

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300

200

100

0

PG

Time (h)

Cel

l cou

nt (m

illio

ns/m

l)

Yeast concentration – all probes

!

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#!

$!

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300

200

100

0

PG

Time (h)

Cel

l cou

nt (m

illio

ns/m

l)

Yeast begins to sediment in cone

at half gravity

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300

200

100

0

PG

Time (h)

Cel

l cou

nt (m

illio

ns/m

l)

Evidence of poor mixing in early primary

fermentation

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PG

Time (h)

Tem

p. (o

C)

Temperature – bottom probes

Relative distribution of yeast in fermenter

Time (h)

Rel

ativ

e pr

opor

tion

(%)

PG

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Cone

Beer

Yeast cropped

VDK spec. achieved and cooling on

Time to PG

50% total yeast in cone

Effect of yeast strain

Strain 1 (moderately flocculent)

Strain 2 (non-flocculent)

Strain 3 (very flocculent)

Conclusions

•  Natural mixing in large fermenters is poor •  Conditions are heterogeneous for most of

fermentation •  Sedimented yeast does not contribute to

VDK removal •  Early sedimentation increases yeast stress

Response

•  Providing a means of stirring should produce faster and more consistent fermentation

•  Discontinuing stirring at the appropriate time will allow the yeast crop to form and this can be removed whilst still warm and before heat and other stresses produce harmful effects

Pumped loop mixing systems

Rotary jet head (ISO-MIX A/S)

Flow meter

Variable speed pump

Rotary mixing head suspended

in wort

Mixing efficiency

•  1m3 pilot scale tank

•  Tank filled with iodine solution

•  Sodium thiosulphate solution added to loop

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Stirring on

All wort in Stirring off

Effect of stirring on yeast distribution using a moderately flocculent strain Pumped loop system in practice

•  Based on trials performed at several commercial breweries

– Reduced cycle times in all cases (10 – 30%) – Significant improvements in cycle time

consistency –  Improvements in ethanol yield

Effect on cycle time duration and consistency

0

5

10

15

20

25

30

35

40

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 170

5

10

15

20

25

30

35

40

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15

Unstirred fermentations

Stirred fermentations

Fermentation Fermentation

Tim

e to

coo

l (da

ys)

•  18.5oPlato wort •  Conical fermenters of various capacities up to 5000 hl •  Recirculation rate 250hl/h

00.20.40.60.81

1.21.41.61.82

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 190

0.20.40.60.81

1.21.41.61.82

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15

Unstirred fermentations

Stirred fermentations

Fermentation Fermentation

Res

idua

l ext

ract

(oP

)

Residual extract

Average increase in ethanol yield – 2.9%

024681012141618

0 4 8 12 16 20 24 28

Time (h)

Unmixed

Mixed

Tem

p (o

C)

Effect of mixing and improved convection on cooling

•  Crash cooling in 1800 hl conical with or without mixing •  Mixing by a single IM 20 RJH operated at ca. 250 hL/h

Conclusions

Implications of heterogeneity

•  Prolonged pitching time and poor mixing gives no precise start-point to fermentation

•  Yeast population with heterogeneous physiology

•  Possible restrictions on passive transport of nutrients and metabolites and into and out of cells

•  Off-line samples are not representative of the whole

•  In consistencies in yeast growth, beer yields and fermentation cycle times

Fermentation management

•  Ensure consistent and controlled onset – Pitch early and over short time period – Apply mixing as soon as possible to disperse

yeast – Dose oxygen in appropriate quantity and at

appropriate time to regulate yeast growth extent and flavour development

•  Could be both pre- and post completion of wort collection

Fermentation management

•  Apply forced mixing throughout primary fermentation

•  Cease mixing at time suitable for particular yeast strain

•  Allow crop to form and remove warm and as soon as possible

•  Mixing regime produces more consistent and higher yielding fermentations

•  Mixing can be used to increase the efficiency of heat transfer from cooling jackets

Thank you for your attention!