Classifications

• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
  • C12C7/00—Preparation of wort
  • C12C7/04—Preparation or treatment of the mash
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
  • C12C7/00—Preparation of wort
  • C12C7/04—Preparation or treatment of the mash
  • C12C7/047—Preparation or treatment of the mash part of the mash being unmalted cereal mash
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
  • C12C11/00—Fermentation processes for beer
  • C12C11/003—Fermentation of beerwort
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
  • C12C5/00—Other raw materials for the preparation of beer
  • C12C5/004—Enzymes
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
  • C12C7/00—Preparation of wort
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E50/00—Technologies for the production of fuel of non-fossil origin
  • Y02E50/10—Biofuels, e.g. bio-diesel

Definitions

• the present invention is concerned with the preparation of fermentable wort from cereal grains, particularly from unmalted cereal grains.
• a further aspect of the invention is a wort obtained by carrying out the process according to the invention.
• the invention is also concerned with fermentation of worts obtained by the process according to the invention, in the production of alcohol, in the distilling industry or in the brewing of beer.
• Background art Beer is manufactured by fermentation of either malted grains or unmalted grains.
• Beverage Industries International (1989), 1, 77-81) propose the addition of enzymes in the brewing of beer from unmalted sorghum, such as alpha-amylase, protease, beta-glucanase, cellulase, fungal alpha-amylase, amyloglucosidase and the like.
• MacFadden et al. also recommend to add yeast food for fermentation when unmalted sorghum is used.
• Bajomo et al. M.F. and Young, T.W., J. Inst. Brew. (1992) 98, 515-523; Bajomo,
• the pH value of the fermentation medium is in the range 4-5 which means that fungal exo-peptidases are not active (Labbe, J.P., Rebeyrotte, P. Biochimie (1974) 56, 839-844, Lehman, K und Uhlig, H. Hoppe Seyler's Z. Physiol. Chem. (1969) 350, 99-104).
• a disadvantage of the above process is, therefore, that under these conditions, the fungal proteases used perform endoproteolysis only, thereby generating mainly oligopeptides and little free amino-acids.
• the present invention provides a process for making wort from unmalted cereal grains with unexpectedly good properties, such as high freely available Nitrogen (hereinafter referred to as FAN), good filterability and yield of the wort.
• FAN high freely available Nitrogen
• the process may also be employed in the manufacture of worts from malted cereals, but it is particularly advantageous for the production of worts from unmalted grains, such as unmalted sorghum, or mixtures of unmalted sorghum and corn.
• unmalted sorghum such as unmalted sorghum
• the advantages are also existent with worts made from malted cereals (such as malted barley) combined with unmalted cereals (such as corn, rice or sorghum), a so-called “mixed brew”.
• the invention provides a process for the production of a fermentable wort from cereal grains, comprising the steps of:
• thermostable exopeptidases such as the fungal amino-pepti ⁇ dases, but also thermostable carboxy-peptidases are useful.
• Particularly preferred accord ⁇ ing to the invention are amino-peptidases endogenous to Aspergillus fungi, more in particular A. niger, A. oryzae or A. sojae.
• the process is particularly useful with a cereal grain which comprises at least 20% unmalted cereal, preferably more than 50% unmalted cereal, such as sorghum grains supplemented with unmalted corn cobs, rice or other unmalted cereals. It is found to be very advantageous according to the invention when the exopeptidase is present during the liquefaction of the cereal grains.
• a fermentable wort is provided which is obtainable by a process according to the invention.
• Yet another aspect of the invention is in a process for brewing beer, wherein a fermentable wort is used according to the invention.
• the invention further provides a process for making an alcoholic beverage, such as beer, comprising the steps of making wort using a process according to the invention and subsequently, or simultaneously, fermenting the said wort, thereby obtaining, e.g. beer.
• a process for enzymatically releasing freely available nitrogen from cereals containing high amounts of glutelin and/or prolamin comprising the step of adding to the grains, or a liquefied mash obtained from said grain, a combination of an endoprotease and an exo-peptidase.
• a process for producing alcohol comprising the step of fermenting the FAN obtained according to the process according to the invention in the presence of a yeast capable of producing alcohol.
• Fig. 1 shows the pH profile of leucine-aminopeptidase from Aspergill s niger
• Fig. 2 shows the pH profile of phenylalanine-aminopeptidase from Aspergillus niger
• Fig. 3 shows the temperature profile both aminopeptidases
• a process for the preparation of a fermentable wort from cereals, wherein at least a protein is present having exo-peptidase activity under the conditions used.
• the aminopeptidases endogenous to fungi, especially the Aspergilli are useful, since they are sufficiently stable and active at pH 5 to 8, which is about the range wherein the pH falls during the liquefaction step.
• carboxypeptidases are less useful.
• carboxy-peptidase may be used advantageously in this step, provided they are sufficiently stable in the temperature range 50 - 60°C, preferably 50 - 70°C.
• exopeptidases does not only lead to an increase of the freely available nitrogen (FAN) of the wort, but also to an improve ⁇ ment of the filterability and the yield of the wort, compared to the process wherein no exopeptidases are used.
• FAN freely available nitrogen
• the process according to the invention is particularly advantageous for the preparation of fermentable wort from unmalted cereals, more in particular unmalted sorghum, optionally supplemented with other cereal material, such as corn, wheat, oat or rice.
• Cereals in the context of this invention includes sorghum, wheat, barley, oat, rice and corn, and the like.
• exopeptidases according to the invention are also advantageous in the case of mixed brews, wherein as a rule malted cereal material as well as unmalted raw cereal material is used, (for example having up to 80%, or even up to 90% of malted cereals, the remainder consisting of unmalted cereals), as it was found that exopeptidases positively influence the organoleptic properties (taste and/or smell). It is envisaged, that these advantages are common to brewing from unmalted as well as malted cereals, as well as mixtures thereof.
• FAN filterability, yield, and organoleptic properties, are those having relatively high prolamin and glutelin protein fractions.
• rice about 80% glutelin belongs to this category. When sorghum is used, attention should be paid that varieties are selected which are relatively low in polyphenol content.
• the preparation of the wort may be carried out as usual. Generally, it comprises the liquefaction of the cereal raw material to obtain a mash, followed by saccharification of the mash to obtain a wort. Filtration prior to fermentation is important.
• the liquefaction step usually comprises grinding of the cereal raw material to obtain a flour of suitable particle size, hydrating with from about 1 to about 4, preferably about 3 parts of water, and optionally, depending on the endoprotease used, from about 50 to about 300 ppm of calcium, preferably 200 ppm Ca 2+ .
• Enzymes from Bacillus stearot- hermophilus appear to be less Calcium-dependent. Consequently, no Ca 2+ supplementation is required in that case.
• the particle size of the ground cereals should not exceed about 3 mm; not more than 3,5% should exceed 1,3 mm; not more than 1,5% should be smaller than 0.25 mm.
• Enzymes that may be used in addition are cellulases, ⁇ -glucanases, and or other plant cell wall degrading enzymes.
• the liquefaction medium is usually adjusted to a pH of between about 5 and 8, preferably between about 6 and 7, using, for example, calcium hydroxide. It is important to add ⁇ -amylase, preferably a thermostable ⁇ -amylase to the liquefaction medium as well as an endoprotease in a dosage sufficient to at least partially liquefy the cereal starch, and to at least partially degrade protein. Suitable dosages of ⁇ -amylase are from about 0,5 to about 2,0, preferably about 1 - 1,5 kg per Ton, when B.A.T.S. is used.
• Suitable dosages of proteases are, in the case of Brewers protease 2000, more than 0.5 kg/Ton grains (kg/T), preferably more than 1 kg/T. In the case of Panstimase 400 more than 2 kg/T, preferably more than 5, more preferably more than 10 kg/T should be used.
• liquefaction process a number of steps are usually carried out at elevated temperature: after adding ⁇ -amylase and protease the mixture is maintained at a tempera ⁇ ture between about 40°C and 65°C, preferably between about 45 and 55°C, most prefe- rably 50°C, until a sufficient liquefaction is obtained.
• the time needed depends on the cereal or mixture of cereals used, but usually from about 30 minutes till about 2 hours is satisfactory.
• the temperature is raised gradually, the rate not being critical, till about 90-95°C and left at that temperature for about 30 minutes to about 1 hour.
• the mixture is cooled to a temperature at which saccharification takes place: usually at about 50°C to about 70°C, preferably between about 55°C and 65°C, most preferably about 60°C. Slightly higher temperatures than 70°C should be possible, depending on the thermostability of the enzymes used in the saccharification step.
• saccharifying enzymes such as Brewers Fermex ( ⁇ - amylase) or Novamyl (recombinant ⁇ -amylase) in amounts usually ranging from about 400 g/T to about 1 kg/T for Brewers Fermex. Also glucoamylases are frequently used.
• the saccharification takes from about 30 minutes to about 2 hours, whereafter the temperature is raised to about 75°C to about 85°C, inter alia to inactivate enzymes and unwanted microorganisms, and kept at the preferred elevated temperature for about 10 minutes; the period is not very critical.
• the mash so obtained is subsequently filtered using equipment well known in the art; a funnel with Schleicher & Schuell paper filter works satisfactorily.
• the wort is fermented by a suitable yeast, under conditions depending on the strain used, and the final purpose; in addition to brewing beer, production of alcohol as biofuel or as alcoholic beverage are envisaged by the instant invention. Suitable strains, and suitable conditions are well known to the person skilled in the art.
• exo-peptidase during the preparation of wort, for example for brewing beer, is especially advantageous during the liquefaction step of the cereal raw material.
• the addition of exo-peptidase during the saccharification step also leads to the mentioned advantages, such as higher FAN-levels, improved filterability and higher yield of the wort.
• the process according to the invention should allow a phase wherein the pH and temperature conditions allow the fungal exo-peptidases to be active.
• Suitable exo-peptida- ses are those endogenous to fungi in general, more in particular those of Aspergillus. It is found that aminopeptidases of Aspergillus species, including A. niger, A. sojae and A. oryzae are especially useful.
• organoleptic properties taste and smell
• beers produced from wort wherein exo-peptidases have been used in the liquefaction step or the saccharification step (or both) are improved. It is envisaged that this advantage is obtained when exo-peptidases is used in beer manufacture from malted cereals, such as traditional barley malts, or mixed brew beers (i.e. from a combination of malted and unmalted cereals).
• the ⁇ -amylase used in the liquefaction step of the process according to the invention is generally an enzyme which cleaves ⁇ -1,4 -glucose-glucose bonds in starch. It is chosen amongst thermostable ⁇ -amylases. Very good results may be obtained with the ⁇ -amylase from Bacillus licheniformis commercially available from Gist-Brocades under the trademark Brewers Amyliq Thermo Stable (B.A.T.S.).
• the endoprotease used in the liquefaction step of the process according to the invention is generally an enzyme which cleaves peptide bonds in proteins under pH and temperature conditions of the beginning of a liquefaction step (pH 5-6 ; t° 45-55°C).
• a liquefaction step pH and temperature conditions of the beginning of a liquefaction step (pH 5-6 ; t° 45-55°C).
• the neutral protease from Bacillus amyloliquefaciens commercially available from Gist-Brocades under the trademark Brewer's Protease 2000.
• the proteolytic enzymes from Streptomyces fradiae may be used, which are commer ⁇ cially available from Panstimase SARL under the trademark Panstimase 400.
• exo-peptidases (liquefaction and/or saccharification)
• the exo-peptidases used in the liquefaction step of the process according to the invention are generally enzymes which cleave N-terminal bonds of peptides or proteins. Very good results may be obtained with preparations from Aspergillus species. A method for obtaining aminopeptidases from Aspergillus niger is disclosed below.
• Exo-peptidase activity is expressed as Leucine aminopeptidase unit or as Phenylalanine aminopeptidase unit:
• 1 Leu-AP unit is the amount of enzyme needed to produce 1 ⁇ mole p-nitroaniline per minute at pH 7,2 and 20°C from L-leucine-p-nitroanilide * Phenylalanine aminopeptidase unit
• 1 Phe-AP unit is the amount of enzyme needed to produce 1 ⁇ mole p-nitroaniline per minute at pH 7,2 and 20°C from L-phenylalanine-p-nitroanilide.
• This activity is measured by the hydrolysis of casein at pH 6.0, 40°C for lh.
• One PU is the amount of enzyme needed to liberate the equivalent of 1 ⁇ mole tyrosine per minute after precipitation of the remaining proteins with trichloracetic acid.
• strains 1108 and 1502 have been obtained from a culture collection and were deposited under the accession numbers NRRL 3112 and CBS 115.39, respectively.
• Strain NRRL 3112 has been used for the production of amyloglucosidase, ⁇ - amylase and glucoamylase.
• Strain CBS 115.39 has been used for the production of amylase.
• Example 2 Some strains from the screening described in Example 1 have been fermented in laboratory fermenters (10 liters). Results obtained with strain 1502 are presented in this Example.
• the following nutrients used were: 100 g/1 maltodextrins, 40 g/1 soy bean flour, 40 g/1 hydrolysed casein, 5 g/1 corn steep, 2 g/1 gelatin, 2 g/1 potassium dihydrogenophosphate, 1.3 g/1 sodium nitrate, 1 g/1 ammonium chloride, 0.01 g/1 iron sulphate and 0.5 g/1 antifoaming agent. All nutrients were firstly mixed together except maltodextrin. pH was adjusted at
• the fermenter was then sterilized at 125°C for 40 minutes.
• the maltodextrin solution was sterilized separately and added to the sterile but cooled fermentation medium.
• the main fermentation was run in a laboratory fermenter which was filled with 6 liters of the medium described above and inoculated with the inoculum flask. Stirring and air providing were adjusted to maintain dissolved oxygen concentration as high as possible. The temperature was maintained at 30°C. The fermentation was stopped when all nutrients had been consumed, i.e. after about 130 hours.
• the fermentation broth was filtrated to remove all microorganisms. Aminopeptida- se and endoprotease activities were measured in the filtrate: 0.15 Leu-AP/ml 1.0 Phe-AP/ml ⁇ 0.05 Val-AP/ml ⁇ 0.1 PU/ml UF concentration was then performed to formulate liquid aminopeptidase, glycerol (50%) being the stabilizing agent.
• the obtained solution called 'Peptidase L2' had the following activities:
• Leu-AP and Phe-AP activities were determined from peptidase L2 (see Example 2) but using different buffers to screen a pH range from 2.5 to 9.0.
• pH profile of leucine-aminopeptidase from Aspergillus niger is shown in Fig. 1.
• pH profile of phenylalanine-aminopeptidase from Aspergillus niger is shown in Fig. 2.
• Leu-AP and Phe-AP activities were determined from peptidase L2 but using different incubation temperatures to screen a temperature range from 5 to 70°C. Temperature profiles are shown in Fig. 3.
• Results show that each enzyme has a different optimal temperature, i.e. 50°C for Leu-AP and 60°C for Phe-AP.
• aminopeptidases from a culture of Aspergillus niger. These aminopeptidases have an optimal activity in a range of pH 6-8 and in a range of temperature of 50-60°C; moreover, under the culture conditions, aminopeptidases can be produced without detectable or substantial amounts of endoprotease.
• aminopeptidases can be produced without detectable or substantial amounts of endoprotease.
• more activity of aminopeptidase is present than exoprotease, preferably 10 times more, more preferably 30 times more.
• the amylase used in the saccharification step of the process according to the invention is an enzyme which cleaves ⁇ -1,4 glucose-glucose bonds in dextrins or starch to yield maltose and/or glucose as the major products.
• Very good results may be obtained with the ⁇ -amylase from Aspergillus oryzae commercially available from Gist-Brocades under the trademark Brewers' Fermex or with the recombinant ⁇ -amylase from Bacillus amyloliquefaciens commercially available from Novo under the trademark Novamyl.
• Exa ple 1 is an enzyme which cleaves ⁇ -1,4 glucose-glucose bonds in dextrins or starch to yield maltose and/or glucose as the major products.
• Very good results may be obtained with the ⁇ -amylase from Aspergillus oryzae commercially available from Gist-Brocades under the trademark Brewers' Fermex or with the recombinant ⁇ -
• Sorghum var. FAFA FARA
• co cobs are ground according to standard specifications for beer production.
• One part grains (60% sorghum + 40% com cobs) is hydrated with 3 parts water.
• Calcium chloride is added in order to warrant 200 ppm total Ca2+ in the liquefaction medium. pH is adjusted to 6,5 with calcium hydroxide.
• B.A.T.S. is added at a dose of 1,5 kg per Ton grains.
• Other proteolytic enzymes are added in amounts shown in Table 2:
• the mixture is maintained at 50°C for lh ; the temperature is then raised up to 95°C (rate l°C/min) and maintained at 95°C for 45 minutes. It is then cooled down to 60°C within 5 minutes. Brewers Fermex is then added (600g/T). The mash is then saccharified at 60°C for 45 minutes. The temperature is then raised up to 76°C and maintained at that temperature for 10 minutes. The mash is poured into a funnel contai ⁇ ning Schleicher and Schuell paper filter. The volume of filtered wort is then measured and its specific gravity is also determined. This allows to calculate extract and yield. Amino-acids are measured with the ninhydrin reagent using glycine as standard. The ami ⁇ no-acids concentrations obtained are corrected for comparison between worts at the same sugar content (12° Plato). Results are presented in Table 3:
• amino-acids composition of each brew has been determined by HPLC. Amino-acids are classified according to the rate of assimilation by Saccharomyces sp. :
• Each wort has been boiled for 45 minutes ; boiled and distilled water has been added aseptically to each wort in order to adjust the sugar content at 12° Plato.
• 350 ml of each standardised wort was poured aseptically into sterile flasks ; brewers' yeast was inoculated in each flask (5 g/1). Fermentations have been run for 8 days at 11 °C. Apparent attenuati ⁇ on of each fermented wort was determined from the density after 8 days fermentation.
• endoprotease + exopeptidase applied to sorghum in the process according to the invention enables to produce worts with satisfactory ability for beer fermentation when compared to worts obtained with malt.
• endoprotease from Bacillus amyloliquefaciens + exo-pep ⁇ tidase from Aspergillus sojae yields an important improvement in Group A + Group B amino-acids content.
• Example 4 This example shows the advantages of introducing exo-peptidases at the liquefac ⁇ tion step rather than at the saccharification step in the process according to the invention.
• Sorghum + co cobs are brewed as described in example 1.
• Brewers Protease 2000 is added at the liquefaction step (1,8 kg/T) in all brews.
• Exo-peptidase from Aspergillus sojae (40000 Leu-AP/T) is added either at the liquefaction step (tests n°l-2) or at the saccharification step (tests n°3-4).
• Standard deviations for volume filtered, yield and amino-acids content have been determined by repeating identical tests. Estimations are : 10 ml, 0,5% and 0,9 mg/1 respectively.
• Example 5 This Example illustrates the effect of increasing doses of exopeptidases from A. oryzae in the brews.
• Sorghum + corn cobs are brewed as described in Example 1. Brewers Protease 2000 and exopeptidase are added at the liquefaction step (Table 11).
• Example 6 This Example illustrates the effect of increasing doses of exopeptidases from A. niger in the brews.
• Sorghum + corn cobs are brewed as described in Example 1. Brewers Protease 2000 and exopeptidase are added at the liquefaction step.
• Example 7 Barley (var. PLAISANT) was ground into fine flour adapted to filter presses in brewhouse. 57g flour is suspended at 50°C for lh in 300ml water containing: 9mg B.A.T.S.
• Barley was brewed as described in Example 7 but replacing the exo-peptidase from Aspergillus sojae by the exo-peptidase from Aspergillus niger.
• CBS Centraalbureau voor Schimmelcultures
• CBS Centraalbureau voor Schimmelcultures

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