6- Pot Stills Flashcards

1
Q

Common features

A

4 elements: heat source, pot where liquid to be distilled placed, condenser, structures (tubing) that link pot & condenser

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2
Q

Direct heat

A

Original method, wood or coal, rustic pot stills for Mezcal, controlling heat accurately requires skill & monitoring, difficult to maintain even heat across base, creates hot spots & can scorch any solids giving off flavours, well-managed heat spots can increase Maillard reactions & contribute flavour

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3
Q

Gas burners

A

Larger scale, legally required for Cognac, some in Scotland for malt whisky, easier to control, burners placed for even heating, scorching solids still an issue- use mechanical scrapers so that solids don’t settle

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4
Q

Indirect steam heating

A

Steam most widely used, cost benefits, easier to control, steam created in boiler, need water & fuel, steam piped into still & never comes in contact with liquid, heat exchange- keeps liquid boiling, as liquid heated steam cools down & condenses so fresh steam constantly introduced, flow rate & temp controlled & quickly adjusted

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5
Q

Coils

A

Steam piped through coiled pipe submerged in liquid, not as common because still issues with scorching

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6
Q

Jackets

A

Most widely used, mounted on outside of pot & provides very even heat over largest surface area, very efficient, lack of hot spots- low chance of scorching, still use mechanical stirrers

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7
Q

Jacket variation

A

Replace steam with boiling water, water directly heated, used by smaller distilleries (steam boiler more $$), not as responsive, water at lower temp so less energy supplied

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8
Q

External heat exchangers

A

Liquid pumped out & recirculated back, ensures large surface area for heating & continual, rapid movement reduces risk of scorching

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9
Q

Steam injection

A

Only option for solid-state fermentation (baijiu), also for liquids with very high solid content (pomace brandies, Grappa), stills have inlet for steam at base, steam introduced at high pressure & forced through material, heat causes volatile fractions to evaporate & pass out top, requires direct contact so quality of steam can impact

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10
Q

Managing reflux

A

Low levels create fuller & richer spirit, amount of reflux in pot still limited

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11
Q

Still height

A

Easiest way to manage reflux, tall stills have cooler still heads & promote more reflux

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12
Q

Lyne arm

A
  • points downward- no further reflux can take place, even if vapours condense in tube they still flow into condenser
  • angled upwards- any condesation can flow back into still & reflux continues until vapours enter condenser
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13
Q

Intensity of the boil

A

Changing heat input is how most control consistency of temp gradient

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14
Q

Plates

A

Rare in traditional pot stills, modern hybrids- purifiers in 2 Scottish distilleries, add reflux in form of vertically-oriented plates on lyne arm

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15
Q

Dephlegmators

A

Rare in traditional stills, common in hybrids

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16
Q

Internal cleaning systems

A

Modern stills have pipes with sprinkler heads or ‘spray balls’, copper gets covered in residue & stops being available for sulfur management, dirty stills can affect quality

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17
Q

Pressure management

A

Pressure changes can damage still & in extreme cases explode, when filled displaces air so hatch or valve needs to be open

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18
Q

Pressure during operation

A

Pressure inside higher so strong enough to withstand, needs safety valve, challenging during 1st distillation when CO2 released (dissolved in fermented liquid)

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19
Q

Pressure when turned off

A

Gases cool & contract so pressure drops creating partial vacuum, valve open to prevent being crushed, emergency anti-collapse valve

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20
Q

Computer controlled

A

Modern stills designed to prevent unsafe conditions

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21
Q

Condensers

A

Heat exchangers that rely on coolant (cold water), most common- shell & tube, worm tub, water constantly introduced at base & taken from top, water leaving is warm & is cooled, vapours enter at top (hottest part) & gradually cooled while passing through coldest part at bottom

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22
Q

Shell and tube

A

Most widely used, coolant passes up condenser through narrow pipes before flowing out top, pipes enclosed in container (shell), vapours enter shell & cooled by contact with cold water pipes

23
Q

Advantages of shell and tube

A

More energy efficient, less space, cooling pipes have larger surface area, made from copper so remove more sulfur compounds, results in lighter & cleaner spirit

24
Q

Scotland

A

1 distillery equipped with 2 shell

& tube condensers, 1 copper & 1 stainless, can vary styles by switching between them (when switched off)

25
Q

Worm tub

A

2 parts: large vat of cold water (tub) & single coiled tube (worm) placed inside vat of water, vapours pass into worm & slowly condense, liquid flows out pipe at bottom

26
Q

Other condensers

A

Rrustic stills (Mezcal, Korea, China & Japan), variation of dephlegmator, placed at top of still & not separate from it, have 1 part- bowl of cold water- constantly flowing & refreshed, bowl sits on top

27
Q

Process of rustic still condensers

A

Hot vapours rise & condense on underside of bowl, some liquid drops back down, some flows along underside of bowl to base & drips into small vessel that feeds a tube, it directs it out & is collected

28
Q

Multiple batch distillation

A

Most distill 2x, some 3x, a handful once

29
Q

Scottish double pot still distillation targets

A

1- raise alcohol from 10% to 40% abv

2- get close to collecting ethanol from original liquid

30
Q

1st distillation

A

1st liquid off is 55-60% abv depending on still, when 40% abv continue because ethanol still in original liquid

31
Q

% abv starts to drop in 1st distillation

A

Continue until abv coming off is 1%, hardly any ethanol left in still, collected liquid about 15% abv, drops because higher prop of ethanol becoming vapour, continues & ethanol in vapours drops too, to collect enough ethanol a large amount of water has to be collected

32
Q

Principal aim of 1st distillation

A

To remove some water & group-4 fractions

33
Q

2 outputs of 1st distillation

A

1- low wines- about 25% abv
2- liquid waste- remains with tiny amount of ethanol, some less volatile fractions & all of non-volatile fractions, some discard, some larger distilleries process as syrup for cattle feed

34
Q

2nd distillation

A

Low wines, heads & tails from previous 2nd distillation placed in still, between 25-30% abv, still is turned on

35
Q

Outputs from the condenser

A

Liquid flowing off 1st has high conc of group-1 fractions (most volatile), also has group-3 fractions (left as residue at end of previous 2nd distillation)

36
Q

Heads

A

Liquid collected for 15-20 minutes, has high amounts of unwelcome fractions, flow redirected into 2nd container, ‘cut’

37
Q

Hearts

A

Collected a few hours depending on size of still & how it’s being operated, high conc of group-2 fractions, another cut made & redirected to container containing heads

38
Q

Tails

A

High conc of group-3 fractions (least volatile), collection continues for several hours until abv is 1%

39
Q

Temperature in the still

A

Gradually increases d/t changing composition, as conc of ethanol & volatile congeners falls, temp rises to 100 C (212 F) (boiling point of water), contributes to rise in conc of group-3 fractions

40
Q

Heads & tails

A

High levels of group-1 & 3 fractions, also contains ethanol & desirable congeners so recycled back with next batch

41
Q

Heart

A

Becomes spirit sold, straight off still is 70% abv

42
Q

Liquid waste

A

Water & group-4 fractions

43
Q

Using cuts to shape style

A

Flow reaches highest conc in order from most volatile to least, vapours at any time are mix, determine what to include & what to exclude

44
Q

Inclusions

A

Group-2 & what wanted to select & conc (narrow cuts), small amounts of group-1 & 3 fractions can give extra dimension (wider cuts)

45
Q

Group-1 fractions

A

Can give attractive aromatic lift

46
Q

Group-3 fractions

A

Can add palate richness & extra complexity

47
Q

Separating fractions

A

Limit, level of separation improved by raising level of reflux, run hotter & reflux reduced- more group-3 fractions will come out

48
Q

Temperature management

A

1- high heat with small difference between top & bottom, quick distillation & high flow rate, peaks of conc compressed, harder to separate group-1 & 3 fractions
2- lower heat, wider temp difference, longer distillation, slower flow gives more separated peaks, easier to exclude group-1 & 3 fractions

49
Q

Exclusions

A

Group-4 fractions excluded (never leave still), separate unpleasant smelling fractions from heart, heads & tails separated & recycled (contain ethanol & group-2 fractions), gin distillers sell them off

50
Q

Advantages of pot stills

A

Reliable, centuries long processes, difficult to reproduce if changes made (ex. stainless- durable & easy to clean but copper has vital role)

51
Q

3 challenges of pot stills

A

Operating costs, inability to make highly rectified spirits, prevent build up of group-3 fractions during extended distillation

52
Q

Operating costs

A

Historically large workforce, many repetitive tasks, time consuming, can be automated, now Scotland distilleries have handful of workers

53
Q

Rectification

A

Triple distillation can reach 80% abv, not possible to go higher, direction of travel is one-way, vapours move from boiling liquid to condenser, amount of reflux & liquid returned to pot are limited, have to include other fractions to conc, with tighter cuts & discarding more this issue remains

54
Q

Eliminating group-3 fractions

A

Recycling heads & tails- get a build up of group-3 fractions, fewer group-1 fractions so not an issue