96% (?) of the solids in brewing wort are carbohydrates. Proteins make up only 3% and the rest are β-glucans, vitamins and minerals. Of the carbohydrates more than 95% are products of the starch conversion that happens in the mash tun. As a result the starch degradation is the main purpose of mashing. It produces fuel that the yeast needs for fermentation from the insoluble starch found in malt and mash tun adjuncts. The extend to which this conversion happens will determine the strength (gravity or extract content) of the produced wort and its fermentability as well as other quality parameteres.
In mashing starch conversion is preceded by gelatinization of the starches. While this is not necessary for conversion, as plants do exactly this when they germinate, it greatly speeds up the process though the exposure of a lot of substrate (amylose and amylopectin) from the starch granule to the starch converting enzymes (mainly α- and β-amylase).
Starch granules are insoluble in cold water and will absorb only little water. The form a suspension that quickly settles once agitation stops. As the water is heated (50+ C) more and more water is absorbed and the granules start to swell [Narziss, 2005]. The water absorbed during this process can be up to 30 times the weight of the starch granule. This uptake of water initially happens within the amorphous growth rings. The granule starch to leach amylose and the crystalline layers break open and separate from the starch granule as gelatenous sheets. At this point the crystalline structure is lost and the process becomes irreversible with respect to the shape of the starch granule [Shetty, 2006]. The starch granule has gelatinized.
While the temperature range during with gelatinization occurs has been found to be quite narrow for individual starch granules (~ 1C) the temperature range between the gelatinization of the first granules and the complete gelatinization of all granules can be quite large. Figure 1 shows the temperature ranges for gelatinization for a number of starches. It can be seen that not all these starches fully gelatinize at temperatures that are encountered in a saccharification rest. If this is not the case they will have to be gelatenized before that rest though either a cereal mash or the use of pre-gelatinized (e.g. flaked) forms. Another interesting aspect is the different gelatinization temperature ranges that have been determined for large and small barley granules. 90% of the starch in barley are large granules which will be gelatenized at saccharification rest temperatures while the rest are small starch granules which may not fully gelatenize until higher temperatures are reached. This effect can explain some of the efficiency benefits that can be gained from a mash-out or a decoction mash.
Gelatinization is a process that requires free water for the swelling and breaking the hydrogen bonds that hold the crystalline structures in place. If free water is limited due to a high concentration of starch (e.g. overly thick mash conditions) less swelling takes place and a melting of the crystalline section needs to occur [Donald, 2004]. This leads to an increase in the gelatinization temperature. This limitation of free water can also be caused by the presence of sugars other dissolved solids. For corn starch it has been shown that a 25% sucrose solution increase the gelatinization temperature from 70 to 78C [Donald, 2004]. This could have been one of the factors why thick mashes showed a lower efficiency compared to thin mashes in the Mashing Experiments.
As starch starts to gelatenize the viscosity of the liquid will increase. This can be noticed in brewing to some extend but by far less that what is commonly seen in cooking. The reason for that is the presence of enzymes (in particular α-amylase) that will start breaking down the amylose and amylopectin molecules as soon as they become accessible. This process reduces the viscosity of the mash and is therefore called liquification [Kunze, 2007]. Liquifying decoctions through a rest at 70-74C before further heating to a boil for example mitigates the risk of scorching the mash during the decoction boil.
A strong increase in viscosity can however become a problem in cereal mashes. Especially when using rice starch which is known to swell very strongly. This can lead to scorching or even the immobilization of mash agitators [Kunze, 2007]. To counteract that some malt should be added to cereal mashes and a short liquification rest might be held between 75 and 80C (just before all the α-amylase gets denatured) before it is then heated to boiling.
The gelatinization temperature also depends on growing conditions and crop year [Kunze, 2007]. And Kessler showed that a weak correlation exists between the VZ 45C malt analysis number and the gelatinization temperature [Kessler, 2008]. VZ 45C is the ratio between the extract that can be extracted through mashing at 45C and the amount that can be extracted with a congress mash. This number is given on some malt analysis sheets. Figure 2 shows the data that was publushed in Brauwelt International. According to Weyermann the VZ45 for their malts can be as low as 35. This may result in a gelatinization temperature as high as 65C. While this temperature should not be a problem when using a single saccharification rest, it can become problematic when a maltose rest is held at 63C at which temp the starch will not be fully gelatenized. If this is the case an extended rest at 65C needs to be held in order to achieve the desired fermenntability of the produced wort.
Enzymatic starch breakdown
Starch conversion in the mash is mainly an enzymatic process and there are 4 types of enzymes that can take part. The 2 best known enzymes are α- and β-amylase. Both work on the α(1-4) glycosidic bonds of the starch and dextrin molecules. Another enzyme is limit dextrinase which is able to break the α(1-6) glycosidic bond that forms the branch points in the amylose molecule. At last there is maltase, an enzyme that can break maltose into two glucose molecules. But because this enzyme is already deactivated by temperatures above 45 C, it generally doesn't play any significant role in mashing.
α-amylase is an enzyme that can cleave any α(1-4) bond in starch and dextrines as except for the ones close to the branch points. This breakage of a glycosidic bond is also called hydrolyzation as it consumes one water molecule. It is the enzyme that is responsible for the rapid loss of viscosity after malt starch gelatinized. A process that is called liquefaction of the mash. While α-amylase is very good at breaking down starch into smaller dextrines, which quickly reduces the iodine reaction from a black-blue to a more reddisch brown color, it is not very good at producing fermentable sugars. This results from the low affinity that α-amylase has towards smaller glucose chains.
β-amylase is much better at producing fermentable sugars. In fact the way in which β-amylase hydrolyzes starches and large dextrines is the reason for the large maltose content in wort produces through mashing. It attaches to the non-reducing end of a glucose chain and clips off one maltose molecule after another. But because it has to do that at the non-reducing end it’s activity has to stop when it comes close to a branch point (α(1-6) link). In order to reach the glucose chains after the branch points it relies on the activity of the α-amylase which creates a non-reducing end every time it splits a glucose chain or the limit dextinase which can break the branching α(1-6) link itself. In mashing α- and β-amylase work in concert: α-amylase creates substrate (i.e. non-reducing ends) for β-amylase. The process of creating sugars is called saccharification and happens mostly after the liquefication of the mash. Mashed that intend to produce a highly fermentable wort always try to maximize the β-amylase activity. This is mainly done through the rest tempearature(s) and the time spent at these rest(s) which will be discussed later
α- and β-amylase alone cannot completely saccharify (i.e. convert to all sugar) starch. The reason for that are α(1-6) that make up 6-7% of the bonds in amylopectin. But malt contains one enzyme that can: limit dextrinase. But the problem with limit dextrinase is that is not as heat stable as α- and β-amylase and quickly denatures at temperatures above 60C. Since at this temperature only little starch may be gelatinized and accessible yet there aren’t many branch points for this enzyme to work on. As a result most brewing wort will contain a large number of limit dextrines which are the branch points that were left behind by α- and β-amylase activity. Unless a very high fermentability is desired the residual dextrines are actually desired as they contribute positively to the character of the beer.
Maltase is an enzyme that has its optimum between 30 and 40 C and can split a single glucose molecule from the non-reducing end of a glucose chain (similar to β-amylase which splits a glucose pair from the non-reducing end of glucose chains). It's affinity to the substrate increases as the degree of polimerization decreases and it is highest for maltose (degree of polimerization is 2) [Kessler, 2006]. But it is generally of little interest in mashing as at its working temperature there is not much maltose present in the wort (given that the mash is doughed in at or below 40 C). If activity of this enzyme is desired to increase the glucose level of the wort the mash needs to be held for saccharification at 63-65C and after having been cooled to 40 C fresh malt is added which also adds new maltase enzymes. After a rest of 30-45 min the mash is heated again to convert the starch that has been added with the new malt. This mash schedule has been introduced by Markus Hermann from the Weihenstephan brewing school to produce high glucose worts for ester rich Weissbiers [Hermann, 2005]
The consumption of one water molecule means that the production of 1 kg maltose (or an equivalent mix of glucose, maltose and larger sugars/dextrines) from starch consumes about 50 ml of water. A typical mash for a 19 liter (5 gal) batch that contains about 3 kg of starch which is converted to mostly fermentable sugars will consume about 150 ml water. This is in the order of 1% of the water added to the mash and generally neglected when calculating the amount of water needed for brewing.
Kunze describes 4 different stages of starch conversion in the mash [Kunze, 2007] (Figure 4). Assuming a low enough dough-in temperature after dough in the starch is present as a suspension of starch granules in water. Once agitation is stopped these starch granules quickly settle. No iodine reaction can be detected yet and the viscosity of the liquid is low. But Amylase enzymes may already attack the starch granules and free and convert some starch. As the temperature is increased the gelatinization temperature of the starch is reached and the granules release their amylose and amylopectin. These large molecules immediately thicken the mash and its viscosity rises sharply. The iodine reaction will be blue-black at this stage. But at this point the amylase (especially the α-amylase) and limit dextrinase enzymes will quickly break the large amylose and amylopectin molecules into large dextrins which greatly reduces the viscosity of the mash. The brewer calls this liquification of the mash. The iodine reaction becomes less blue and more reddish brown as an indication that the size of the glucose chains is reduced. As the dextrines become smaller β-amylase and limit dextrinase become more important in efficienctly reducing them to mostly fermentable sugars as the α-amylase only shows a low affinity towards these smaller dextrines. This stage is called saccharification and is completed when the iodine completely disappears.
Effect of mashing conditions
Mashing conditions like temperature, time, water/grist ratio pH and others affect the complex interactions between the enzymes and the substrate and have an effect on the quality of the produced wort. Through a control of these conditions the brewer can greatly influence the wort composition and the final character of the beer. In addition to that mashing conditions also have an effect on the amount of extract that is created from the grist and will determine how well it is utilized. These are reasons why a brewer should have a good understanding on how mashing effects the wort and later the beer.
The following sections will evaluate the effect of the various mash parameters in detail.
Temperature and Time
|Enzymne||optimum temperature||optimum pH|
Mashing consists of a series of temperature rests held for specific times. In it's simplest form only one such rest is held. This type of mashing is called isothermal or single infusion mashing. The temperatures and times for these rest(s) is chosen such that certain enzymes are allowed to work on the grist in a controlled manner. The effects of temperature and time on enzymatic catalyzed reactions, like mashing, were discussed in the article about Enzymes. It has been shown that the optimum temperature for a particular enzyme is not a constant but that it is dependent on the time that this enzyme is allowed to work. The lower the temperature the longer is the enzyme active and the more product can be produced by the enzyme if given enough time.
While it has been shown that mashes at 55C (131F) can recover up to 90% of the potential extract even though they are well below the gelatinization temperature of the starch in the grist the temperature(s) of the saccharification rest(s) are generally chosen such that the starch is able to gelatenize. This allows for a more effective use of the enzymes.
The mash temperature and time has a direct impact on the fermentability of the wort produced by mashing. This fermentability (or attenuation potential) is the ratio between the fermentable sugars (mainly glucose, maltose and maltotriose) to the total amount of extract. Since most of the extract are carbohydrates anyway the fermentability is directly linked to the balance between fermentable and unfermentable starch degradation products. And this balance is controlled by controlling the intensity of the β-amylase and limit dextrinase activity. Both these enzymes are more heat liable than α-amylase (see Table 1) and this fact is used in controlling their activity especially in isothermal mashes.
|Highest Extract (mostly starch conversion)||65-68||149-154.4|
|Fastest saccharification (dextrinization)||70||158|
|Highest yield of fermentable extract||65||149|
|Highest percentage fermentability||63||145.4|
|Maximum activity of α-amylase||70||158|
|Maximum activity of β-amylase||60||140|
The longer the β-amylase and limit dextrinase are allowed to work the more fermentable the resulting wort will be. In isothermal mashes this is controlled by the temperature. The higher the temperature the faster the β-amylase will be denatured and the less fermentable sugars are produced. At lower temperatures these enzymes will be able to work for a longer time and will produce more fermentable sugars. But because of the lower temperature these reactions will take longer and a longer mash may be necessary to achieve a sufficient conversion of the starch. Note that some α-amylase activity is necessary to provide enough non-reducing ends (especially beyond the branch points in amylopectin) for the β-amylase but that even at temperatures below the α-amylase's optimum enough activity exists to provide that. A dependency between wort fermentability and rest temperature has been shown in the Mashing Experiments. In multi step saccharification rests like the German Hochkurz mash, the fermentability is mostly controlled through the length of the maltose rest which is held at 60-64 C (140-148F).
Figure 6 shows the progress of extract and fermentable extract in isothermal mashes at 3 different temperatures. It is evident that the higher temperature mashes quickly reach a saturation of the produced extract. This is a result of the limited amount of starch that is available in the mash and the fact that there are more than enough enzymes (largely α-amylase) to convert it into soluble compounds. Only for the 60C mash does the rise in extract lag begind significantly. This is the result of only partial starch gelatinization and slower enzymatic reaction speed at this temperature. But it keeps rising and should eventually approach the levels that were reached earlier by the higher temperature mashes.
The fermentable extract shows a different dependency on the temperature. The higher the mash temperature the quicker the level of fermentable extract levels off and remains constant. This is a result of the quicker denaturing of the β-amylase and limit dextrinase. After 180 min mashing the mash at 65C still leads the mash at 60C with respect to the amount of fermentable extract generated but it starts to level off and the mash at 60C is expected to generate more fermentable extract than the mash at 65C if the mashing time is extended past 180F.
While the discussion was for idealized enzymatic reactions, which are different from what is happening in the mash the Temperature section of the Enzymes article shows graphs that are very similar to the data shown in Figure 4 which supports the theory that the fermentability is controlled through the time that the β-amylase and limit dextrinase are allowed to act.
pH and brewing water
|characteristic||pH at mash temp||pH of a cooled sample|
|shortest saccharification time||5.3||5.7|
|greatest extract obtained||5.2-5.4||5.55 - 5.75|
|greatest extract from a decoction mash||5.3-5.6||5.65 - 5.95|
|maximum α-amylase activity||5.3||5.7|
|maximum β-amylase activity||5.1-5.3||5.4-5.6|
|maximum phytase activity||5.2||5.5|
As discussed in Enzymes - The effect of pH the pH of the mash has a significant impact on the enzyme activity and since mashing is mostly an enzymatic reactions it requires the pH to be in an acceptable range. Within that range the pH can also be used to control the reaction of the individual enzymes.
Mashing experiments Have shown that an unoptimal pH results in lower extract production and less fermentable wort. The optimal mash pH ranges are shown in Table 3.
A major confusion that commonly arises in the discussion of mash pH is that it changes with temperature. Mashes behave like weak acids and they disassociate more (i.e. free more H+ ions) as the temperature rises. It has been shown that the pH of a mash at 65C is about 0.35 pH units lower than its pH at room temperature (25C) and about 0.45 pH units lower at mash out temperatures (75C) [Briggs, 2004]. The pH optimum of α-amylase has been determined at 5.3 in room temperature experiments. But it mashing its optimum is commonly reported to be 5.7. The reason for this is that the mash pH is commonly measured in a cooled sample of the mash. Measurement at mash temperatures is possible but common pH testing equipment like test strips and pH meters are designed for pH measurement in cooled samples.
The proper mash pH does more than allowing for optimal enzyme activity it also provides the basis for the boil and cast-out wort pH. The boil pH tends to be at or slighly higher than the mash pH and the cast-out wort pH is 0.1 - 0.2 units lower than the boil pH.
water to grist ratio
preparation of the grist
- [Valclavik] Vickie A. Valclavik, Elizabeth W. Christian, Essentials of Food Science, Third Edition, Springer
- [Champe] Pamela C, Champe, Richard A. Harvey, Denise R. Ferrier, Biochemistry, Lippincott's Illustrated Reviews
- [Kunze, 2007] Wolfgang Kunze, Technologie Brauer und Maelzer, 9. Auflage, VLB Berlin
- [Narziss, 2005] Prof. Dr. agr. Ludwig Narziss, Prof. Dr.-Ing. habil. Werner Back, Abriss der Bierbrauerei, Technische Universitaet Muenchen (Fakultaet fuer Brauwesen, Weihenstephan). WILEY-VCH Verlags GmbH Weinheim Germany, 2005
- [Donald, 2004] A. M. Donald, Understanding Starch Stucture and Functionality, Chapter 5 in Starch in Food: Structure, Function and Applications By Ann-Charlotte Eliasson, CRC Press, 2004
- [Shetty, 2006] Kalidas Shetty, Food Biotechnology, CRC Press, 2006
- [Kessler, 2008] Dr.-Ing. Matthias Thaddäus Keßler, Analytische Erfassung und Interpretation der Stärkedegradation im Gersten- und Malzkorn und die Aussagekraft für den Brauprozess, Dissertation, Technische Universität München, 2006
- [TU Vienna] www.vt.tuwien.ac.at/scripts/172942/172942_Brauerei_04.pdf