Transport kinetics of maltotriose in strains ofSaccharomyces

Summary Maltotriose transport was studied in two brewer's yeast strains, an ale strain 3001 and a lager strain 3021, using laboratory-synthesized¹⁴C-maltotriose. The maltotriose transport systems preferred a lower pH (pH 4.3) to a higher pH (pH 6.6). Two maltotriose transport affinity systems have been indentified. The high affinity system hasK _m values of 1.3 mM for strain 3021 and 1.4 mM for strain 3001. The low affinity competitively inhibited by maltose and glucose withK _i values of 58 mM and 177 mM. respectively, for strain 3021, and 55 mM and 147 mM, respectively, for strain 3001. Cells grown in maltotriose and maltose had higher maltotriose and maltose transport rates, and cells grown in glucose had lower maltortriose and maltose transport rates. Early-logarithmic phase cells transported glucose faster than either maltose or maltotriose. Cells harvested later in the growth phase had increased maltotriose and maltose transport activity. Neither strain exhibited significant differences with respect to maltose and maltotriose transport activity.     

Maltotriose fermentation by Saccharomyces cerevisiae

Maltotriose, the second most abundant sugar of brewer's wort, is not fermented but is respired by several industrial yeast strains. We have isolated a strain capable of growing on a medium containing maltotriose and the respiratory inhibitor, antimycin A. This strain produced equivalent amounts of ethanol from 20 g l⁻¹ glucose, maltose, or maltotriose. We performed a detailed analysis of the rates of active transport and intracellular hydrolysis of maltotriose by this strain, and by a strain that does not ferment this sugar. The kinetics of sugar hydrolysis by both strains was similar, and our results also indicated that yeast cells do not synthesize a maltotriose-specific α-glucosidase. However, when considering active sugar transport, a different pattern was observed. The maltotriose-fermenting strain showed the same rate of active maltose or maltotriose transport, while the strain that could not ferment maltotriose showed a lower rate of maltotriose transport when compared with the rates of active maltose transport. Thus, our results revealed that transport across the plasma membrane, and not intracellular hydrolysis, is the rate-limiting step for the fermentation of maltotriose by these Saccharomyces cerevisiae cells. Journal of Industrial Microbiology & Biotechnology (2001) 27, 34–38. Received 13 January 2001/ Accepted in revised form 29 May 2001     

Mechanisms of action of the α-amylase of Micromonospora melanosporea

The -amylase of Micromonospora melanosporea was produced extracellularly during batch fermentation in a 5.0-1 fermentor. The absence of an organic nitrogen source in its growth medium facilitated subsequent purification of the enzyme by ammonium sulphate fractionation and two consecutive Superose-12 gel-filtration steps. The enzyme exhibited maxima for activity at pH 7.0 and 55° C and was 72% stable at pH 6.0–12.0 for 30 min at 40° C. It had a relative molecular mass of 45 000 and an isoelectric point at pH 7.6. The enzyme catalyses the conversion of starch to maltose (53%, w/w) as the predominant final end-product. Initial hydrolysis of this substrate, however, gave rise to the formation of maltooligosaccharides in the range maltotriose to maltohexaose. Maximum yields of these intermediate sugars accumulated to between 31 and 42% (w/w) as the reaction proceeded. The action of the M. melanosporea amylase on high concentrations of saccharides larger than maltotriose resulted in the formation of mainly maltose and maltotriose without concomitant glucose production. A combination of hydrolytic and transfer events is postulated to be responsible for this phenomenon and for the high maltose levels achieved. Correspondence to: C. T. Kelly     

Improved Fermentation Performance of a Lager Yeast after Repair of Its AGT1 Maltose and Maltotriose Transporter Genes

The use of more concentrated, so-called high-gravity and very-high-gravity (VHG) brewer''s worts for the manufacture of beer has economic and environmental advantages. However, many current strains of brewer''s yeasts ferment VHG worts slowly and incompletely, leaving undesirably large amounts of maltose and especially maltotriose in the final beers. α-Glucosides are transported into Saccharomyces yeasts by several transporters, including Agt1, which is a good carrier of both maltose and maltotriose. The AGT1 genes of brewer''s ale yeast strains encode functional transporters, but the AGT1 genes of the lager strains studied contain a premature stop codon and do not encode functional transporters. In the present work, one or more copies of the AGT1 gene of a lager strain were repaired with DNA sequence from an ale strain and put under the control of a constitutive promoter. Compared to the untransformed strain, the transformants with repaired AGT1 had higher maltose transport activity, especially after growth on glucose (which represses endogenous α-glucoside transporter genes) and higher ratios of maltotriose transport activity to maltose transport activity. They fermented VHG (24° Plato) wort faster and more completely, producing beers containing more ethanol and less residual maltose and maltotriose. The growth and sedimentation behaviors of the transformants were similar to those of the untransformed strain, as were the profiles of yeast-derived volatile aroma compounds in the beers.The main fermentable sugars in brewer''s wort are maltose (ca. 60% of the total), maltotriose (ca. 25%), and glucose (ca. 15%). In traditional brewery fermentations, worts of about 11° Plato (°P) are used, corresponding to a total fermentable sugar concentration of about 80 g · liter⁻¹. Many modern breweries ferment high-gravity worts (15 to 17°P), and there are efforts to raise the concentration to 25°P, corresponding to a total sugar concentration of about 200 g · liter⁻¹. Industrial use of such very-high-gravity (VHG) worts is attractive because it offers increased production capacity from the same-size brew house and fermentation facilities, decreased energy consumption, and decreased labor, cleaning, and effluent costs (34, 35).Whereas glucose, which is used first, is transported into yeast cells by facilitated diffusion, the α-glucosides maltose and maltotriose are carried by proton symporters (2, 26, 39). Maltose transport seems to have a high level of control over the fermentation rate. Thus, during the early and middle stages of fermentation of brewer''s wort by a lager yeast, the specific rate of maltose consumption was the same as the specific zero-trans maltose uptake rate measured off line with each day''s yeast in each day''s wort spiked with [¹⁴C]maltose (27). Furthermore, introducing a constitutive MAL61 (maltose transporter) gene into a brewer''s yeast on a multicopy plasmid accelerated the fermentation of high-gravity worts (17). Maltotriose is the last sugar to be used in brewing fermentations, and significant amounts of residual maltotriose sometimes remain in beer, causing economic losses (lower yield of ethanol on wort carbohydrate) and possibly undesirable organoleptic effects. The problem of residual sugars in beer is more serious when high-gravity and VHG worts are used. Some, but not all, maltose transporters can also carry maltotriose. The MALx1 genes (x = 1 to 4 and 6) encode transporters that carry maltose efficiently but are generally believed to have little or no activity toward maltotriose (1, 3, 13, 30), although substantial activity toward maltotriose was reported by Day et al. (4). Some yeast strains contain a gene 57% identical to MAL11 that is usually known as AGT1 but is recorded in the Saccharomyces Genome Database (SGDB) as MAL11. The Agt1 transporter has relatively high activity toward maltotriose, as well as maltose (13), and similar K_m values (4 to 5 mM) for these two substrates (4). Alves et al. (1) found that the specific deletion of AGT1 from several Saccharomyces cerevisiae strains also containing at least one MALx1 gene (MAL21, MAL31, and/or MAL41) abolished their ability to transport maltotriose but did not decrease their maltose transport activity. These results supported the belief that the Mal21, Mal31, and Mal41 transporters cannot carry maltotriose, though it remains possible that there are differences between Malx1 transporters from different strains. The same group has also shown (33) that overexpression of AGT1 on a multicopy plasmid in an industrial yeast strain with a very limited ability to ferment maltotriose provided the strain with increased maltotriose uptake activity and the ability to ferment maltotriose efficiently. In 2005, a novel kind of α-glucoside transporter was independently found by two groups (6, 30) in some industrial strains of brewer''s, baker''s, and distiller''s yeasts. These transporters are coded by MTT1 (also called MTY1) genes, which are 90 and 54% identical to the MAL31 and AGT1 genes, respectively. The Mtt1 transporters have high activity toward maltotriose and are the only known α-glucoside transporters with lower K_m values for maltotriose than for maltose (30).Before the discovery of the MTT1 genes, Vidgren et al. (36) sequenced AGT1 genes from two apparently unrelated lager strains and two apparently unrelated ale strains of brewer''s yeast. Surprisingly, at that time (because other maltotriose transporters were not known), the AGT1 genes from the lager strains contained an insertion of one nucleotide, resulting in a premature stop codon, and encoded a truncated, nonfunctional 394-amino-acid polypeptide, whereas those from the ale strains encoded full-length 616-amino-acid transporters. This premature stop codon was later shown (37) to be present in AGT1 genes from all eight of the lager strains tested but was not in any of the four ale strains tested, whereas MTT1 genes were present in all of the lager strains tested but in none of the ale strains tested.In the present work, we have tested whether lager fermentations can be accelerated and residual maltotriose levels decreased by repairing the defective AGT1 genes of lager strains with appropriate DNA sequences from ale strains. Furthermore, the MALx1 and AGT1 genes are repressed by glucose and induced by α-glucosides (9, 16, 19, 25), so that replacing the native AGT1 promoter with a constitutive S. cerevisiae promoter might also increase α-glucoside transport activity and accelerate wort fermentations. The objectives of the present work were to confirm that α-glucoside transport has a high level of control over the rate and extent of wort fermentation and to create a genetically modified lager yeast strain that has improved fermentation performance but contains only Saccharomyces DNA.     

Enzyme formation by a yeast cell wall lytic Arthrobacter species: formation of amylase

The kinetics of amylolytic enzyme formation by a yeast cell wall lytic Arthrobacter species were studied. Cultivation on autoclaved cells of baker's yeast showed that amylase formation was closely related to trehalose and glycogen dissimilation. Growth on yeast glycogen (0.5%) proceeded quite rapidly ( = 0.31 h^–1) with extensive amylase formation during exponential cell multiplication and a further low increase in activity during the stationary phase. Beside amylolytic activity [450 units (U) l^–1] the formation of a relatively high level of -glucosidase (90 U l^–1) was detected, the latter almost exclusively bound to bacterial cells. Growth on 0.5% trehalose occurred at a reduced rate ( = 0.22 h^–1) with post-logarithmic enzyme synthesis in the stationary phase. Amylase activity attained a level of 1200 U l^–1, whereas -glucosidase was very low at 7.7 U l^–1. Continuous culture experiments in the chemostat showed maximal volumetric productivity of amylase (105 U l^–1 h^–1) at a dilution rate of 0.15 h^–1. Growth on various carbohydrates revealed low levels of amylolytic activity (<100 U l^–1), which were increased by a -1,4-glucans and oligosaccharides such as starch, dextrin, maltotriose and maltose. On 0.5% maltose, growth-associated enzyme synthesis (230 U l^–1) was detected at a reduced growth rate ( = 0.14 h^–1). Amylolytic enzyme preparations from the culture fluid showed an unusual cleavage pattern; acting on starch, the polymer was almost completely hydrolysed to maltotriose and maltose in a molar ratio of 3:1.Correspondence to: W. A. Hampel     

The alternate respiratory pathway of Candida albicans

Candida albicans contains a cryptic cyanide and antimycin A insensitive respiratory system. This alternate oxidase was found (i) at all growth rates from =0.05 to 0.26 in a chemostat culture and (ii) in both mycelial and yeast forms of the organism. Neither chloramphenicol nor cycloheximide prevented the expression of the alternate oxidase. Salicyl-hydroxamic acid was a potent inhibitor of the cyanide insensitive respiration. The respiration of mitochondria grown in the presence of antimycin A was not inhibited by cyanide or antimycin A but was inhibited by salicylhydroxamic acid.Abbreviations KCN potassium cyanide - SHAM salicyl hydroxamic acid     

Development of medium components for the production of glucosyl-transferring enzyme by Aureobasidium

Aureobasidium sp. ATCC 20524 produced a glucosyl-transferring enzyme which produced panose (O--D-glucopyranosyl-(1»6)-O--D-glucopyranosyl-(1»4)-d-glucose) from maltose. Optimum production for the enzyme was with maltose at 2% (w/v) and yeast extract at 1.5% (w/v). Enzymatic activity reached 0.7×10³ U/g dry cells after 48 h.     

Maltotriose metabolism by Saccharomyces cerevisiae

Saccharomyces cerevisiae grew slower but reached higher cellular densities when grown on 20 g maltotriose l^–1 than on the same concentration of glucose or maltose. Antimycin A (3 mg l^–1) prevented growth on maltotriose, but not on glucose or maltose, indicating that it is not fermented but is degraded aerobically. This was confirmed by the absence of ethanol and glycerol production. Active uptake of maltotriose across the plasma membrane is the limiting step for metabolism, and the low rate of maltotriose transport observed in maltotriose-grown cells is probably one of the main reasons for the absence of maltotriose fermentation by S. cerevisiae cells.     

Transport of maltose by Pseudomonas fluorescens W

The system for uptake of maltose in Pseudomonas fluorescens W was inducible. Using a mutant strain unable to hydrolyze maltose, it was shown that maltose was taken up unaltered against a concentration gradient. Uptake of ¹⁴C maltose was only significantly inhibited by nonradioactive maltose or maltotriose. These were the only sugars that could displace accumulated radioactive maltose in the strain unable to hydrolyze maltose. Uptake exhibited saturation kinetics and was inhibited by energy poisons, indicating that this system was one of active transport. Sulfhydryl-binding reagents reversibly inhibited maltose uptake. No transport ability was lost when cells were subjected to osmotic shock. Using the protein-binding dye 7-diazonium-1,3-naphthalene disulfonate a protein or proteins located in or external to the cell membrane was implicated in maltose transport. The hydrolysis of p-nitrophenyl--D-glucoside (PNPG) was used as an indirect measure of transport ability since penetration of PNPG, not its hydrolysis, was the rate-limiting step.Abbreviations PNPG paranitrophenyl--D-glucoside - NDS 7-diazonium-1,3-naphthalene disulfonic acid - PMB p-hydroxymercuribenzoate - MBS p-chloromercuriphenylsulfonic acid - PCMB p-chloromercuribenzoate - CCCP carbonyl cyanide m-chlorophenylhydrazone - DNP 2,4-dinitrophenol - HOQNO 2-heptyl-4-hydroxyquinoline-N-oxide     

The high maltose-forming α-amylase ofSaccharomonospora viridis: mechanisms of action

Summary The thermophilic actinomycete,Saccharomonospora viridis produces a thermostable -amylase which forms 63% (w/w) maltose on hydrolysis of starch. Maltotriose and maltotetraose are the only intermediate products observed during this reaction, with maltotriose accumulating to 40% (w/w). Both unimolecular and multimolecular mechanisms (transfers and condensation) have been shown to occur during the concentration-dependent degradation of maltotriose and maltotetraose. Such reactions result in the almost exclusive formation of maltose from maltotriose at high initial concentration. These mechanisms of action result in the production of the high levels of maltose obtained upon hydrolysis of starch and related substrates.     

The high maltose-producing α-amylase of the thermophilic actinomycete,Thermomonospora curvata

The -amylase of Thermomonospora curvata catalyses the formation of very high levels of maltose from starch (73%, w/w) without the attendant production of glucose. The enzyme was produced extracellularly in high yield during batch fermentation in a 5-1 fermentor. Purification was achieved by ammonium sulphate fractionation, Superose-12 gel filtration and DEAE-Sephacel ionexchange chromatography. The enzyme exhibited maxima for activity at pH 6.0 and 65°C, had a relative molecular mass of 60900–62000 and an isoelecric point at 6.2. The exceptionally high levels of maltose produced and the unique action pattern exhibited on starch and related substrates indicate a very unusual maltogenic system. The predominance of maltose as the final end-product may be explained by the participation of reactions other than simple hydrolysis and the preferential cleavage of maltotriose from higher maltooligosaccharides. The enzyme exhibits very low affinity for maltotriose (K _m=7.7 × 10^–3 m) and its conversion to maltose is achieved by synthetic followed by hydrolytic events, which result in the very high levels of maltose observed and preclude glucose formation. This system is distinguished from other very high maltose-producing amylases by virtue of its high temperature maximum, very low affinity for maltotriose and the absence of glucose in the final saccharide mixture. Correspondence to: C. T. Kelly     

Production of chitinolytic enzymes from a novel species ofAeromonas

A bacterial strain secreting potent chitinolytic activity was isolated from shrimp-pond water by enrichment culture using colloidal crab-shell chitin as the major carbon source. The isolated bacterium, designated asAeromonas sp No. 16 exhibited a rod-like morphology with a polar flagellum. Under optimal culture conditions in 500-ml shaker flasks, it produced a chitinolytic activity of 1.4 U ml^–1. A slightly higher enzymatic activity of 1.5 U ml^–1 was obtained when cultivation was carried out in a 5-liter jar fermentor using a medium containing crystalline chitin as the carbon source. The secretion of the enzyme(s) was stimulated by several organic nitrogenous supplements. Most carbon sources tested (glucose, maltose, N-acetylglucosamine, etc) enhanced cell growth, but they slightly inhibited enzyme secretion. Glucosamine (0.5% w/v) severely inhibited cell growth (16% of the control), but it did not significantly affect enzyme secretion. The production of chitinolytic enzymes was pH sensitive and was enhanced by increasing the concentration of colloidal chitin to 1.5%. The observed chitinolytic activity could be attributed to the presence of -N-acetylglucosaminidase and chitinase. Chitinase was purified by ammonium sulfate fractionation and preparative gel electrophoresis to three major bands on SDS-PAGE. An in-gel enzymatic activity assay indicated that all three bands possessed chitinase activity. Analysis of the enzymatic products indicated that the purified enzyme(s) hydrolyzed colloidal chitin predominantly to N,N-diacetyl-chitobiose and, to a much lesser extent, the mono-, tri, and tetramer of N-acetylglucosamine, suggesting that they are mainly endochitinases.     

High maltose-producing amylolytic system of a Streptomyces sp.

The -amylases of Streptomyces sp. IMD 2679 produced yields of 79% (w/w) maltose from starch by reactions other than simple hydrolysis. The enzymes also had a low affinity (Km 8.0–8.2 mm) for maltotriose and each possessed a temperature maximum in the range 60–65°C.     

Growth and butyric acid production by Clostridium populeti

The growth of Clostridium populeti in 2% (w/v) glucose medium containing 0.2% (w/v) yeast extract was optimal with 10 mM NH₄Cl as the nitrogen source. Although the maximum specific growth rate (=0.32 h^-1) with 5 mM NH₄Cl was similar, the biomass yield was about 30% lower than that at the optimum. Either sodium sulphide or cysteine-HCl at an optimum concentration of 0.33 mM and 5.0 mM respectively, could serve as the sole sulphur source for growth. The growth rate was unaffected by initial glucose concentrations of up to 10% (w/v), but in the presence of 15% glucose it declined by about 35%. The molar yield of butyric acid (mol/mol glucose) declined from 0.70 in 1% (w/v) initial glucose medium to 0.39 in 10% glucose medium. In 5.7% initial glucose medium, butyric acid levels of 6.3 g/l were obtained (0.56 mol butyrate/mol glucose) after 72 h of incubation in 2.5 l batch cultures. A decrease of about 50% in the maximum specific growth rate of C. populeti was observed in the presence of an initial concentration of either 1.2 g/l of butyric acid or 18.9 g/l of acetic acid.This paper is issued as NRCC No. 29032     

Changes in concentrations of soluble carbohydrates during germination of <Emphasis Type="Italic">Amaranthus caudatus</Emphasis> L. seeds in relation to ethylene,gibberellin A<Subscript>3</Subscript> and methyl jasmonate

Unimbibed Amaranthus caudatus seeds were found to contain stachyose, raffinose, verbascose, sucrose, galactinol, myo-inositol, glucose and fructose, while no galactose, maltose and maltotriose was detected. During imbibition, seed concentrations of verbascose, stachyose, raffinose, galactinol, myo-inositol (temporary) and fructose (transient) were observed to decrease; concentrations of galactose and maltose remained fairly constant, while those of sucrose, glucose and maltotriose increased, the increase in sucrose concentration was only temporary. Effects of gibberellin A₃ (GA₃) at 3 × 10⁻⁴ M and ethephon at 3 × 10⁻⁴ M alone or in the presence of methyl jasmonate (Me-JA) at 10⁻³ M on concentrations of soluble sugars during germination of A. caudatus seeds were examined. Me-JA was found to inhibit seed germination and fresh weight of the seeds, but did not affect sucrose, myo-inositol, galactose and maltose concentrations during imbibition for up to 20 h. The exogenously applied GA₃ was observed to enhance germination, stachyose breakdown and glucose concentration after 20 h of incubation. Ethephon stimulated seed germination as well as utilisation of stachyose, galactinol (both after 14 and 20 h) and raffinose (after 14 h of incubation). Although the stimulatory effect of either GA₃ or ethephon on seed germination was blocked by Me-JA; these stimulators increased mobilisation of raffinose and stachyose, but only ethephon enhanced both glucose and fructose after 14 and/or 20 h of incubation in the presence of Me-JA. The maltose concentration was increased by both GA₃ and ethephon alone and in the presence of Me-JA. Of the growth regulators studied, ethephon alone and/or in combination with Me-JA significantly increased the concentrations of glucose, fructose, galactose, maltose and maltotriose. The differences in sugar metabolism appear to be linked to ethylene or GA₃ applied simultaneously with Me-JA.     

Production of high-purity isomalto-oligosaccharides syrup by the enzymatic conversion of transglucosidase and fermentation of yeast cells

A method for the production of high-purity isomalto-oligosaccharides (IMO) involving the transglucosylation by transglucosidase and yeast fermentation was proposed. The starch of rice crumbs was enzymatically liquefied and saccharified, and then converted to low-purity IMO syrup by transglucosylation. The low-purity IMO produced either from rice crumbs or tapioca flour as the starch source could be effectively converted to high-purity IMO by yeast fermentation to remove the digestible sugars including glucose, maltose, and maltotriose. Both Saccharomyces carlsbergensis and Saccharomyces cerevisiae were able to ferment glucose in the IMO syrup. Cells of S. carlsbergensis harvested from the medium of malt juice were also able to ferment maltose and maltotriose. A combination of these two yeasts or S. carlsbergensis alone could be used to totally remove the digestible sugars in the IMO, coupled with the production of ethanol. The resultant high-purity IMO, including mainly isomaltose, panose, and isomaltotriose made up more than 98% w/w of the total sugars after a 3-day fermentation. When the low-purity IMO was produced from the starch of tapioca flour, 3-day fermentation under the same conditions resulted in IMO with purity lower than that from rice crumbs. For low-purity IMO from rice crumbs, fermentation with washed S. carlsbergensis cells harvested at log phase was the most effective. However, for the low-purity IMO from tapioca flour, incubation with S. cerevisiae for the first 24 h and then supplementing with an equal amount of S. carlsbergensis cells for further fermentation was the most effective approach for producing high-purity IMO.     

Active transport of proline into washed cells of Rhodopseudomonas sphaeroides f. sp. denitrificans grown with nitrate

Washed cells of Rhodopseudomonas sphaeroides f. sp. denitrificans, prepared from cultures grown anaerobically in light with NO ₃ ^- as the terminal acceptor, readily incorporated [¹⁴C]-proline both in light and in the dark. The proline uptake was coupled to the reduction of either NO ₃ ^- , NO ₂ ^- , N₂O or O₂. Light stimulated the accumulation of proline in these cells. The addition of NO ₃ ^- to washed cells in light decreased the K _m for proline from 40 M to 5.7 M. Proline transport was inhibited by antimycin A, 2-n-heptyl-4-hydroxyquinoline-N-oxide both in light and in the dark with nitrate indicating that electron transfer from both denitrification and photosynthesis are involved in this uptake. Inhibition by carbonyl cyanide-m-chlorophenyl hydrazone and 2.4-dinitrophenol indicate that proline transport is energy dependent. The H⁺/proline stoichiometry increased from 1 to 2.5 when the external pH was increased from 6.0 to 8.0. Under these conditions pro increased but p decreased markedly above pH 7.0.Abbreviations TPP⁺ Tetraphenylphosphonium bromide - EDTA ethylenediamine-tetra-acetic acid - CCCP carbonyl cyanide-m-chlorophenyl hydrazone - DNP 2,4-dinitrophenol - HOQNO 2-n-heptyl-4-hydroxyquinoline-N-oxide - DBMIB dibromo-methyl-isopropyl-p-benzoquinone - DCCD N,N-dicyclohexylcarbodiimide     

The Thr505 and Ser557 residues of the AGT1-encoded alpha-glucoside transporter are critical for maltotriose transport in Saccharomyces cerevisiae

Aims:  The main objective of this study was to identify amino acid residues in the AGT1‐encoded α‐glucoside transporter (Agt1p) that are critical for efficient transport of maltotriose in the yeast Saccharomyces cerevisiae. Methods and Results:  The sequences of two AGT1‐encoded α‐glucoside transporters with different efficiencies of maltotriose transport in two Saccharomyces strains (WH310 and WH314) were compared. The sequence variations and discrepancies between these two proteins (Agt1p_WH310 and Agt1p_WH314) were investigated for potential effects on the functionality and maltotriose transport efficiency of these two AGT1‐encoded α‐glucoside transporters. A 23‐amino‐acid C‐terminal truncation proved not to be critical for maltotriose affinity. The identification of three amino acid differences, which potentially could have been instrumental in the transportation of maltotriose, were further investigated. Single mutations were created to restore the point mutations I505T, V549A and T557S one by one. The single site mutant V549A showed a decrease in maltotriose transport ability, and the I505T and T557S mutants showed complete reduction in maltotriose transport. Conclusions:  The amino acids Thr⁵⁰⁵ and Ser⁵⁵⁷, which are respectively located in the transmembrane (TM) segment TM¹¹ and on the intracellular segment after TM¹² of the AGT1‐encoded α‐glucoside transporters, are critical for efficient transport of maltotriose in S. cerevisiae. Significance and Impact of the Study:  Improved fermentation of starch and its dextrin products, such as maltotriose and maltose, would benefit the brewing and whisky industries. This study could facilitate the development of engineered maltotriose transporters adapted to starch‐efficient fermentation systems, and offers prospects for the development of yeast strains with improved maltose and maltotriose uptake capabilities that, in turn, could increase the overall fermentation efficiencies in the beer and whisky industries.