Lecture date: June 27 2025; focus: Beer brewing as a case-study of large-scale fermentation.
Beer production = one of the oldest and largest global biotechnology industries.
Bridges earlier lecture on large-scale cell culture → real-world industrial example.
Emphasis throughout: Identify where enzyme catalysis, microbial physiology, and process engineering intersect.
Carbonated, alcoholic beverage (but note low & 0-Alc variants).
Visual markers
Colour span: very pale → amber → deep brown/black.
Persistent foaming head distinguishes beer from most other drinks.
Liquid clarity varies: bright → protein/yeast haze → intentionally cloudy styles.
Taste/aroma
Bitterness from hop iso-α-acids.
Floral/citrus/herbal notes from hop oils + minor yeast metabolites (higher alcohols, esters).
Mild acidity because dissolved CO2 ↔ H2CO_3.
Water.
Malt (almost always malted barley, occasionally wheat, rye, oats, etc.).
Hops (whole cones or processed extracts).
Yeast (Saccharomyces cerevisiae – “ale” strains; S. pastorianus – “lager” strains).
Worldwide practice allows extra fermentables ("adjuncts" = cane sugar, corn, rice syrup), fruits, herbs, exogenous enzymes (e.g. β-glucanase) for process aid or flavour.
Annual value: >$700 billion (figure slightly dated, still indicative).
Largest producer volumes: China > USA.
Highest per-capita consumption: Czech Republic (long-standing #1).
Growth niches (last 10–15 y): craft breweries, non-/low-alcohol beers.
Water + Malt + Hops + Yeast (+Adjuncts/Enzymes)
↓
Milling → Mashing → Lauter/Word Recovery → Wort Boil (add hops) → Whirlpool/Clarify → Cool & Aerate
↓
Fermentation (Ale or Lager) ↘CO2 ↘Excess Yeast
↓ (Vegemite, extracts)
Maturation → Filtration/Clarification → Packaging (bottle/can/keg)
↓ ↘Pasteurise (in-package or flash)
Waste streams (spent grain, trub) → Animal feed, disposal
Everything prior to fermenter = “upstream”.
Product polishing & packaging = “downstream”.
CO₂ co-product captured as food-grade gas for beverage dispense, carbonation, etc.
Beer ≈ 90\text{–}98\% water → sensory & process impacts huge.
Treatments employed:
Adjust hardness (Ca²⁺, Mg²⁺) → influences mash pH, enzyme activity, flavour.
Particle filtration + UV sterilisation when microbial load questionable.
In high-gravity brewing the dilution water is pre-carbonated with reclaimed CO_2.
“Malt” = barley grain steeped → germinated → kilned.
Steeping: hydrate to ~45\% moisture.
Germination (3–5 days): enzyme synthesis (α- & β-amylase, protease, β-glucanase).
Kilning: stops growth, sets colour/flavour (Maillard reactions) → scale of heat = colour spectrum (pilsner → crystal → chocolate → black malt).
Trade-offs: Darker kilning = richer flavour/colour but denatures more endogenous enzymes → necessitates blend of pale + specialty malts.
Grain received at brewery is first milled/cracked to expose endosperm while keeping husk mostly intact (acts as filter aid later).
Goal: convert insoluble starch → fermentable sugars + extract proteins/minerals.
Operations
Mix milled malt (plus solid adjuncts) with hot liquor (brewing water) → porridge-like mash.
Temperature schedule (typical):
35\,°\text{C} – β-glucanase window (cell-wall breakdown).
45\,°\text{C} – protease rest (AA/peptide formation, foam & clarity control).
62\text{–}66\,°\text{C} – β-amylase (maltose generation).
70\text{–}72\,°\text{C} – α-amylase (dextrin reduction, body).
75\,°\text{C} mash-out (stabilises composition, lowers viscosity).
Enzyme provenance: exclusively from malt unless brewery supplements with commercial enzymes (common in high-adjunct recipes).
Equipment: Lauter tun or mash filter.
Husk bed forms self-filter; sweet wort drawn off under slight vacuum or by pump.
“Sparging” = showering grain bed with 75\,°\text{C} water to rinse residual sugars → increases brewhouse yield.
Solids generated: Spent grain (protein-/fibre-rich) → cattle feed.
Carried out in kettles (copper or modern stainless). Typical 60–90 min vigorous boil.
Functions
Sterilise wort.
Precipitate hot break (protein denaturation, tannin complexes).
Evaporate undesirable volatiles (e.g. DMS from precursor S-methyl-methionine).
Isomerise α-acids from hops → bitterness.
Concentrate wort (≈8 % volume loss).
Hop scheduling
Early additions (“bittering hops”) – maximise iso-α-acid yield.
Late/whirlpool additions (“aroma hops”) – preserve volatile terpenes.
Tangential inlet sets fluid into rotation; solids migrate to centre “trub cone”.
Clear wort drawn from periphery bottom outlet.
Heat-exchanger cools to fermentation set-point (ales 18\text{–}22\,°\text{C}, lagers 8\text{–}15\,°\text{C}).
Only time oxygen is wanted: injected/sterile-air-sparged to ~8\text{–}10\,mg\,L^{-1} O₂ to permit fatty-acid/sterol synthesis for yeast membranes.
Strain choice shapes beer style:
Ale (S. cerevisiae): top-cropping, ester-forward, warmer & faster (≈3–5 d).
Lager (S. pastorianus): bottom-settling/flocculent, clean profile, cooler & slower (≈7–14 d).
Inoculum sources
Serial repitching: harvest cone yeast, acid-wash (~pH 2) → reuse 3-10 cycles until genetics or contamination drifts.
Pure-culture propagation: if contamination rises or strain refresh required, work back from cryostock.
Cylindro-conical tanks dominate; internal agitation = CO₂ lift only.
Key constraints
Optimal metabolic temp < optimal growth temp (high temps → off-flavours).
pH naturally falls to ~4.0\text{–}4.5 → suppresses pathogens.
Ethanol tolerance critical; brewing strains withstand \sim10\text{–}15\%\,(v/v).
Stoichiometry core:
\mathrm{C6H{12}O6 \;\rightarrow\; 2\,C2H5OH + 2\,CO2}
⇒ 1 mol ethanol ↔ 1 mol CO₂ (minimum; biomass diverges some carbon).
Typical time-course (≈4 d ale):
Monosaccharides (glucose, fructose) disappear first (<36 h).
Maltose exhausted by ~60 h.
Maltotriose partly remains → residual body/carbs.
Yeast growth peaks then flocculates; ethanol plateaus.
Cold storage (lagering) 0\text{–}4\,°\text{C} for days–weeks.
Smooths flavour (diacetyl reduction), clarifies via further yeast/protein precipitation, increases CO₂ absorption.
Filtration media: kieselguhr (DE), sheets, membranes.
Additives occasionally used: PVPP (polyphenol binding), silica gels (protein haze control).
Pasteurisation options
Tunnel – bottles/cans heated ~60\,°\text{C} for prescribed “pasteurisation units”.
Flash – heat to 71\,°\text{C} for ~15 s, then package aseptically (common for kegs).
Note: Pasteurisation ≠ sterilisation; just lowers bioburden for shelf-life extension.
Bottles (amber/green glass limits light-struck "skunk" reactions of hop compounds).
Aluminium cans (light-tight, lightweight, recyclable).
Stainless kegs for draught; product flash-pasteurised inline.
CO₂ (food-grade) – captured, compressed, reused/sold.
Spent grain/trub – high protein & fibre → cattle feed; emerging valorisation (biogas, protein isolates).
Surplus yeast – processed into spreads (e.g. Vegemite/Marmite) or nutraceuticals.
Effluent (wort kettle condensate, cleaning-in-place solutions) must meet discharge regulations; breweries integrate anaerobic digesters.
Consumer demand growth ⇒ technological innovation.
Methods
Vacuum distillation – lower boiling point of ethanol.
Reverse osmosis – membrane separates ethanol + aroma condensate from water; re-blend sans alcohol.
Biological – use non-traditional yeasts (e.g. Torulaspora delbrueckii) or limit fermentable sugars to keep <0.5\% ABV.
Process tweaks – arrested fermentation, dealcoholisation post-ferment.
Challenge: maintain body, foam, hop aroma once ethanol removed.
Light exposure → hop iso-α-acids + riboflavin → MBT (“skunky”) – mitigated by brown glass/cans.
Oxygen pickup post-ferment → stale cardboard flavours (trans-2-nonenal).
Low pH, ethanol & hop iso-acids impart natural microbial hurdle; yet Lactobacillus & wild yeasts can still spoil if hygiene lapses.
Enzyme technology – endogenous vs. commercial additions; temperature/pH optimisation.
Microbial physiology – oxygen requirements, ethanol tolerance, contamination control.
Stoichiometry & kinetics – sugar utilisation hierarchy, product yields, growth-associated vs. non-growth-associated metabolism.
Process integration – upstream media prep ↔ fermentation ↔ downstream clarification & packaging.
Sustainability – CO₂ capture, by-product valorisation, water reuse.
Parallels with pharmaceutical cell culture: sterility demands, scale-up constraints, media design (C:N balance).
Enzyme immobilisation & industrial proteases – concepts transferable to detergent, dairy industries.
Bioreactor design fundamentals (mass transfer, heat removal) reappear in bioethanol, kombucha, kimchi, etc.
Public health: responsible drinking campaigns, non-alcoholic options broaden inclusivity.
Regulatory compliance (e.g., Reinheitsgebot, excise taxation) affects formulation freedom.
Environmental stewardship: breweries adopt circular-economy practices (spent grain → food/energy; CO₂ capture) to reduce footprint.
Cultural heritage: brewing traditions (Czech, German, Belgian) illustrate intersection of science & societal identity.
Beer global value: >$700 Bn.
Composition: 90\text{–}98\% water.
Cytology: Yeast optimum growth 30\text{–}35\,°\text{C} but quality demands cooler fermentation (ales 18\text{–}22, lagers 8\text{–}15).
CO₂ : Ethanol stoichiometry 1:1 molar (see equation above).
Fermentation timeframes: ales 3–5 d, lagers 7–14 d + conditioning.
Pasteurisation: ~60\,°\text{C} for 20–30 min (tunnel) or 71\,°\text{C} for 15 s (flash).
Identify four core ingredients & their biochemical roles.
Be able to sketch/annotate the full brewing process flow with upstream & downstream steps.
Explain how mash temperature profile tailors fermentable vs. non-fermentable sugar spectrum.
Write balanced fermentation equation and relate to co-product capture.
Contrast ale vs. lager fermentation in terms of yeast, temperature, flavour output.
Describe at least two technologies for producing low/zero-alcohol beer.
Discuss how hop compounds contribute to both flavour and microbial stability.