Citric Acid Production from Hydrolysate of Pretreated Straw Cellulose by Yarrowia lipolytica SWJ-1b Using Batch and Fed-Batch Cultivation

In this study, crude cellulase produced by Trichoderma reesei Rut-30 was used to hydrolyze pretreated straw. After the compositions of the hydrolysate of pretreated straw were optimized, the study showed that natural components of pretreated straw without addition of any other components such as (NH₄)₂SO₄, KH₂PO₄, or Mg²⁺ were suitable for citric acid production by Yarrowia lipolytica SWJ-1b, and the optimal ventilatory capacity was 10.0 L/min/L medium. Batch and fed-batch production of citric acid from the hydrolysate of pretreated straw by Yarrowia lipolytica SWJ-1b has been investigated. In the batch cultivation, 25.4 g/L and 26.7 g/L citric acid were yields from glucose and hydrolysate of straw cellulose, respectively, while the cultivation time was 120 hr. In the three-cycle fed-batch cultivation, citric acid (CA) production was increased to 42.4 g/L and the cultivation time was extended to 240 hr. However, iso-citric acid (ICA) yield in fed-batch cultivation (4.0 g/L) was similar to that during the batch cultivation (3.9 g/L), and only 1.6 g/L of reducing sugar was left in the medium at the end of fed-batch cultivation, suggesting that most of the added carbon was used in the cultivation.     

Selection and characterization of a newly isolated thermotolerant Pichia kudriavzevii strain for ethanol production at high temperature from cassava starch hydrolysate

Pichia kudriavzevii DMKU 3-ET15 was isolated from traditional fermented pork sausage by an enrichment technique in a yeast extract peptone dextrose (YPD) broth, supplemented with 4 % (v/v) ethanol at 40 °C and selected based on its ethanol fermentation ability at 40 °C in YPD broth composed of 16 % glucose, and in a cassava starch hydrolysate medium composed of cassava starch hydrolysate adjusted to 16 % glucose. The strain produced ethanol from cassava starch hydrolysate at a high temperature up to 45 °C, but the optimal temperature for ethanol production was at 40 °C. Ethanol production by this strain using shaking flask cultivation was the highest in a medium containing cassava starch hydrolysate adjusted to 18 % glucose, 0.05 % (NH₄)₂SO₄, 0.09 % yeast extract, 0.05 % KH₂PO₄, and 0.05 % MgSO₄·7H₂O, with a pH of 5.0 at 40 °C. The highest ethanol concentration reached 7.86 % (w/v) after 24 h, with productivity of 3.28 g/l/h and yield of 85.4 % of the theoretical yield. At 42 °C, ethanol production by this strain became slightly lower, while at 45 °C only 3.82 % (w/v) of ethanol, 1.27 g/l/h productivity and 41.5 % of the theoretical yield were attained. In a study on ethanol production in a 2.5-l jar fermenter with an agitation speed of 300 rpm and an aeration rate of 0.1 vvm throughout the fermentation, P. kudriavzevii DMKU 3-ET15 yielded a final ethanol concentration of 7.35 % (w/v) after 33 h, a productivity of 2.23 g/l/h and a yield of 79.9 % of the theoretical yield.     

Comparison of agarophytes (Gelidium, Gracilaria, and Gracilariopsis) as potential resources for bioethanol production

This study explores the possibility of producing ethanol using the acid hydrolysate of three abundant agar-containing red seaweeds (agarophytes): Gelidium amansii, Gracilaria tenuistipitata, and Gracilariopsis chorda. The main component in the seaweed samples was agar, which ranged from 20 to 51 % (g g^?1 dry weight). After optimizing acid hydrolysis, 100 g of seaweed was hydrolyzed at 130 °C for 15 min with 0.2 M H₂SO₄. Then, 120 mL of a 1:2 mixture of the hydrolysate broth and basal medium was fermented in a 200-mL bottle at 30 °C for 96 h. Of the three seaweeds, G. amansii had the best ethanol yield, producing 0.23 g g^?1 of galactose or 45 % of the theoretical yield. This yield increased to 60 % after detoxification of the hydrolysate with activated carbon.     

Preparation of squid skin collagen hydrolysate as an antihyaluronidase,antityrosinase, and antioxidant agent

A collagen was isolated from squid skin, a processing waste product. The biofunctional activities of enzymatic squid skin collagen hydrolysates were determined to produce a value-added material. Five low-molecular-mass hydrolysate fractions, F1 (>30 kD), F2 (10–30 kD), F3 (3–10 kD), F4 (1–3 kD), and F5 (<1 kD), were manufactured from its enzymatic hydrolysate by ultrafiltration. Fraction F3 had the strongest antihyaluronidase inhibitory activity. Gly, Val, and Pro were major amino acids in F3, while Met, Tyr, and His were minor ones. The molecular mass of F3 was in the range of 3.4 to 10 kD. F3 exhibited copper chelating ability in a concentration-dependent manner. The ferrous chelating ability of F3 was almost 50% at 200 µg/mL. F3 also inhibited tyrosinase activity by 39.65% at 1 mg/mL. Furthermore, F3 had stronger hydroxyl radical scavenging activity (IC₅₀ = 149.94 µg/mL) than ascorbic acid (IC₅₀ = 212.94 µg/mL). Therefore, the squid collagen hydrolysate can be utilized as a nutraceutical or cosmeceutical agent.     

Evaluation of hardboard manufacturing process wastewater as a feedstream for ethanol production

Waste streams from the wood processing industry can serve as feedstream for ethanol production from biomass residues. Hardboard manufacturing process wastewater (HPW) was evaluated on the basis of monomeric sugar recovery and fermentability as a novel feedstream for ethanol production. Dilute acid hydrolysis, coupled with concentration of the wastewater resulted in a hydrolysate with 66 g/l total fermentable sugars. As xylose accounted for 53 % of the total sugars, native xylose-fermenting yeasts were evaluated for their ability to produce ethanol from the hydrolysate. The strains selected were, in decreasing order by ethanol yields from xylose (Y _p/s, based on consumed sugars), Scheffersomyces stipitis ATCC 58785 (CBS 6054), Pachysolen tannophilus ATCC 60393, and Kluyveromyces marxianus ATCC 46537. The yeasts were compared on the basis of substrate utilization and ethanol yield during fermentations of the hydrolysate, measured using an HPLC. S. stipitis, P. tannophilus, and K. marxianus produced 0.34, 0.31, and 0.36 g/g, respectively. The yeasts were able to utilize between 58 and 75 % of the available substrate. S. stipitis outperformed the other yeast during the fermentation of the hydrolysate; consuming the highest concentration of available substrate and producing the highest ethanol concentration in 72 h. Due to its high sugar content and low inhibitor levels after hydrolysis, it was concluded that HPW is a suitable feedstream for ethanol production by S. stipitis.     

S9A Serine Protease Engender Antigenic Gluten Catabolic Competence to the Human Gut Microbe

The human gut microbiome has a significant role in host physiology; however its role in gluten catabolism is debatable. Present study explores the role of human gut microbes in gluten catabolism and a native human gut microbe Cellulomonas sp. HM71 was identified. SSU rDNA analysis has described human gut microbiome structure and also confirmed the permanent residentship of Cellulomonas sp. HM71. Catabolic potential of Cellulomonas sp. HM71 to cleave antigenic gluten peptides indicates presence of candidate gene encoding biocatalytic machinery. Genome analysis has identified the presence of gene encoding S9A serine protease family—prolyl endopeptidase, with Ser591, Asp664 and His685 signature residues. Cellulomonas sp. HM71 prolyl endopeptidase activity was found optimal at pH 7.0 and 37 °C with a K_M of 35.53 μmol and specifically cleaves at proline residue. Current study describes the gluten catabolism potential of Cellulomonas sp. HM71 depicting possible role of human gut microbes in gluten catabolism to confer resistance mechanisms for the onset of celiac diseases in populations with gluten diet.     

Expression of Bacillus pumilus keratinase rK27 in Bacillus subtilis: enzyme application for developing renewable flocculants from bone meal

In this study thermostable keratinase rK₂₇ of Bacillus pumilus KS12 was expressed and secreted in Bacillus subtilis WB980 expression system under the control of xylose promoter (PxylA). The concentration of the recombinant keratinase rK₂₇ produced by B. subtilis reached 4,432 U/mL after 24 h of culture at 37 °C and 200 rpm with 0.5 % xylose at an initial concentration of 0.3 OD_600nm. Using the one-factor-at-a-time approach, we achieved an improvement in enzyme yield of up to 3.4-fold (15,390 U/mL) in the presence of 3 % yeast extract and 0.5 % tryptone. The enzyme was purified to homogenity using nickel affinity chromatography with a 3.63-fold purity and 80 % recovery. The purified enzyme rK₂₇ hydrolyzed 1 g bone meal after 12 h at 40 °C, pH 9, with a maximum protein release of 37.3 mg/g bone meal; in comparison subtilisin Carlsberg hydrolyzed 19.3 mg/g bone meal and proteinase K hydrolyzed 6.2 mg/g bone meal. The hydrolysate obtained after hydrolysis of bone by rK₂₇ was found to be effective as a flocculant at 0.1 mg in a 10 % (w/v) kaolin solution when compared with hydrolysates obtained from substilisin Carlsberg and proteinase K, which were effective at 0.5 mg and >2 mg, respectively.     

Xylan-hydrolyzing thermotolerant <Emphasis Type="Italic">Candida tropicalis</Emphasis> HNMA-1 for bioethanol production from sugarcane bagasse hydrolysate

Sugarcane bagasse is one of the low-cost substrates used for bioethanol production. In order to solubilize sugars in hemicelluloses like xylan, a new thermotolerant isolate of Candida tropicalis HNMA-1 with xylan-hydrolyzing ability was identified and characterized. The strain showed relative tolerance to high temperature. Our results demonstrated 0.211 IU ml^?1 xylanase activity at 40 °C compared to 0.236 IU ml^?1 at 30 °C. The effect of high temperature on the growth and fermentation of xylose and sugarcane bagasse hydrolysate were also investigated. In both xylose or hydrolysate medium, increased growth was recorded at 40 °C. Meanwhile, the efficiency of ethanol fermentation was adversely affected by temperature since yields of 0.088 g g^?1 and 0.076 g g^?1 in the xylose medium, in addition to 0.090 g g^?1 and 0.078 g g^?1 in the hydrolysate medium were noticed at 30 °C and 40 °C, respectively. Inhibitory compounds in the hydrolysate medium demonstrated negative effects on fermentation and productivity, with maximum ethanol concentration attained after 48 h in the hydrolysate, as opposed to 24 h in the xylose medium. Our data show that the newly thermotolerant isolate, C. tropicalis HNMA-1, is able to efficiently ferment xylose and hydrolysate, and also has the capacity for application in ethanol production from hemicellulosic sources.     

Co-fermentation of cassava waste pulp hydrolysate with molasses to ethanol for economic optimization

Cassava waste pulp (CWP)–enzymatic hydrolysate was co-fermented with molasses (CWP-EH/molasses mixture) with the aim to optimize ethanol production by Saccharomyces cerevisiae TISTR 5606 (SC 90). The optimal fermentation conditions for ethanol production using this mixture were 245 g/L initial total sugar supplemented with KH₂PO₄ (8 g/L), at 30 °C for 48 h of fermentation under an oxygen-limited condition with agitation at 100 rpm, producing an ethanol concentration of 70.60 g/L (0.31 g ethanol/g total sugar). The addition of cassava tuber fiber (solid residue of CWP after enzymatic hydrolysis) at 30 g/L dry weight to the CWP-EH/molasses mixture increased ethanol production to 74.36 g/L (0.32 g ethanol/g total sugar). Co-fermentation of CWP-EH with molasses had the advantage of not requiring any supplementation of the fermentation mixture with reduced nitrogen.     

Thermostable alkaline protease from Thermomyces lanuginosus: optimization,purification and characterization

A serine alkaline protease (EC.3.4.21) was isolated, purified and characterized from culture filtrate of the thermophilic fungus Thermomyces lanuginosus Tsiklinsky. Fructose (1.5 %) and gelatin (0.5 %) proved to be the best carbon and nitrogen sources, giving a maximum enzyme yield of 9.2 U/mL. Dates waste was utilized as a sole organic source to improve enzyme productivity, and the yield was calculated to be 11.56 U/mL. This yield was expressed also as 231.2 U/g of assimilated waste. The alkaline protease produced was precipitated by iso-propanol and further purified by gel filtration through Sephadex G-₁₀₀ and ion exchange column chromatography on diethyl amino ethyl (DEAE)-cellulose with a yield of 30.12 % and 13.87-fold purification. The enzyme acted optimally at pH 9 and 60 °C and had good stability at alkaline pH and high temperatures. The enzyme possessed a high degree of thermostability and retained full activity even at the end of 1 h of incubation at 60 °C. Michaelis–Menten constant (K _m), maximal reaction velocity (V _max) and turnover number (K _cat) of the purified enzyme on gelatin as a substrate were calculated to be 4.0 mg/mL, 18.5 U/mL and 1.8 s^?1, respectively. The best enzyme activators were K⁺, Ca²⁺ and Mn², respectively, while phenylmethylsulfonyl fluoride (PMSF) was the strongest inhibitory agent, thus suggesting that the enzyme is a serine type protease. The enzyme is a glycoprotein with molecular mass of 33 kDa as determined by SDS-PAGE. It retained full activity after 15 min incubation at 60 °C in the presence of the detergent Ariel, thus indicating its suitability for application in the detergent industry.     

Production of biobutanol from acid-pretreated corncob using Clostridium beijerinckii TISTR 1461: Process optimization studies

Corncob is a potential feedstock in Thailand that can be used for fermentable sugar production through dilute sulfuric acid pretreatment and enzymatic hydrolysis. To recover high amounts of monomeric sugars from corncob, the sulfuric pretreatment conditions were optimized by using response surface methodology with three independent variables: sulfuric acid concentration, temperature, and time. The highest response of total sugars, 48.84 g/L, was found at 122.78°C, 4.65 min, and 2.82% (v/v) H₂SO₄. With these conditions, total sugars from the confirmation experiment were 46.29 g/L, with 5.51% error from the predicted value. The hydrolysate was used as a substrate for acetone–butanol–ethanol fermentation to evaluate its potential for microbial growth. The simultaneous saccharification and fermentation (SSF) showed that C. beijerinckii TISTR 1461 can generate acetone–butanol–ethanol products at 11.64 g/L (5.29 g/L acetone, 6.26 g/L butanol, and 0.09 g/L ethanol) instantly using sugars from the hydrolysed corncob with Novozymes 50013 cellulase enzyme without an overliming process.     

Biohydrogen production from wheat straw hydrolysate by dark fermentation using extreme thermophilic mixed culture

Hydrolysate was tested as substrate for hydrogen production by extreme thermophilic mixed culture (70°C) in both batch and continuously fed reactors. Hydrogen was produced at hydrolysate concentrations up to 25% (v/v), while no hydrogen was produced at hydrolysate concentration of 30% (v/v), indicating that hydrolysate at high concentrations was inhibiting the hydrogen fermentation process. In addition, the lag phase for hydrogen production was strongly influenced by the hydrolysate concentration, and was prolonged from approximately 11 h at the hydrolysate concentrations below 20% (v/v) to 38 h at the hydrolysate concentration of 25% (v/v). The maximum hydrogen yield as determined in batch assays was 318.4 ± 5.2 mL‐H₂/g‐sugars (14.2 ± 0.2 mmol‐H₂/g‐sugars) at the hydrolysate concentration of 5% (v/v). Continuously fed, and the continuously stirred tank reactor (CSTR), operating at 3 day hydraulic retention time (HRT) and fed with 20% (v/v) hydrolysate could successfully produce hydrogen. The hydrogen yield and production rate were 178.0 ± 10.1 mL‐H₂/g‐sugars (7.9 ± 0.4 mmol H₂/g‐sugars) and 184.0 ± 10.7 mL‐H₂/day L_reactor (8.2 ± 0.5 mmol‐H₂/day L_reactor), respectively, corresponding to 12% of the chemical oxygen demand (COD) from sugars. Additionally, it was found that toxic compounds, furfural and hydroxymethylfurfural (HMF), contained in the hydrolysate were effectively degraded in the CSTR, and their concentrations were reduced from 50 and 28 mg/L, respectively, to undetectable concentrations in the effluent. Phylogenetic analysis of the mixed culture revealed that members involved hydrogen producers in both batch and CSTR reactors were phylogenetically related to the Caldanaerobacter subteraneus, Thermoanaerobacter subteraneus, and Thermoanaerobacterium thermosaccharolyticum. Biotechnol. Bioeng. 2010;105: 899–908. © 2009 Wiley Periodicals, Inc.     

Overproduction of poly(β-malic acid) (PMA) from glucose by a novel Aureobasidium sp. P6 strain isolated from mangrove system

After over 100 strains of Aureobasidium spp isolated from mangrove system were screened for their ability to produce poly(β-malic acid) (PMA), it was found that Aureobasidium sp. P6 strain among them could produce high level of Ca²⁺-PMA. Fourteen percent glucose and 6.5 % CaCO₃ in the medium were the most suitable for Ca²⁺-PMA production. Then, 100.7 g/l of Ca²⁺-PMA was produced using Aureobasidium sp. P6 strain within 168 h at flask level. During 10-l batch fermentation, when the medium contained 12.0 % glucose, 98.7 g/l of Ca²⁺-PMA in the culture and 14.7 g/l of cell dry weight were obtained within 156 h, leaving 0.34 % reducing sugar in the fermented medium. When glucose concentration in the fermentation medium was 14.0 %, 118.3 g/l of Ca²⁺-PMA in the culture and 16.4 g/l of cell dry weight were obtained within 168 h, leaving 0.4 % reducing sugar in the fermented medium. After purification of Ca²⁺-PMA from the culture and acid hydrolysis of the pure Ca²⁺-PMA, analysis of HPLC showed that Aureobasidium sp. P6 strain only produced two main components of Ca²⁺-PMA and minor amount of calcium malate and that the hydrolysate of PMA was mainly composed of calcium malate. This is the first time to report that the novel yeast strain Aureobasidium sp. P6 strain isolated from the mangrove systems can produce such high amount of Ca²⁺-PMA.     

Production of hydrolysate with antioxidative activity by enzymatic hydrolysis of extruded corn gluten

Hydrolysate of extruded corn gluten with higher solubility and antioxidative property was prepared. Extrusion and starch removal of corn gluten were applied as pretreatment before enzymatic hydrolysis by Alcalase. The amylase hydrolysis of starch at 70°C for 3 h resulted in the removal of the starch from the extruded corn gluten. The best hydrolysis results can be obtained by conducting the hydrolysis at 60°C with water addition 20 g/g protein, enzyme addition 0.048 Ansen units/g protein, pH 8.5, and 120 min. Degree of hydrolysis of extruded and nonextruded corn gluten reached 39.54 and 31.16%, respectively, under the optimal condition. Sodium dodecyl sulfate polyacrylamide gel electrophoresis of the optimal hydrolysate revealed that proteolysis of extruded corn gluten was more extensive than proteolysis of its counterpart which was not subjected to extrusion. The molecular weight of the peptides in the optimal hydrolysate was mainly over 3,710–660 Da as determined by gel filtration chromatography. The hydrolysates displayed good solubility and antioxidative activity. The separation profile of the hydrolysate on an ion exchange chromatography of Q-Sepharose Fast Flow showed that many kinds of peptides had antioxidative effect. A new peptide with antioxidative activity was purified, and its amino acid sequence was Phe-Pro-Leu-Glu-Met-Met-Pro-Phe, which was identified by Q-TOF2 mass spectrometry.     

Production of bioethanol using lignocellulosic hydrolysate by the white rot fungus <Emphasis Type="Italic">Hohenbuehelia</Emphasis> sp. ZW-16

A novel white rot fungus strain Hohenbuehelia sp. ZW-16 was identified and first used for bioethanol production in this study. It was found that the strain could produce bioethanol with glucose, xylose and arabinose under limited oxygen condition. Then, corn straw hydrolysate and corncob hydrolysate (mainly composed of glucose, xylose, and arabinose) were used for bioethanol production; the former substrate could produce more bioethanol in the experiment. The optimal sugar concentration and nitrogen sources were selected (50 g/L corn straw hydrolysate and 10 g/L soybean meals, respectively) and the maximum yield of bioethanol reached 4.6 g/L after 8 days of fermentation.     

The Evaluation of Dipeptidyl Peptidase (DPP)-IV, α-Glucosidase and Angiotensin Converting Enzyme (ACE) Inhibitory Activities of Whey Proteins Hydrolyzed with Serine Protease Isolated from Asian Pumpkin (Cucurbita ficifolia)

In the present study, whey protein concentrate (WPC-80) and β-lactoglobulin were hydrolyzed with a noncommercial serine protease isolated from Asian pumpkin (Cucurbita ficifolia). Hydrolysates were further fractionated by ultrafiltration using membranes with cut-offs equal 3 and 10 kDa. Peptide fractions of molecular weight lower than 3 and 3–10 kDa were further subjected to the RP-HPLC. Separated preparations were investigated for their potential as the natural inhibitors of dipeptidyl peptidase (DPP-IV), α-glucosidase and angiotensin converting enzyme (ACE). WPC-80 hydrolysate showed higher inhibitory activities against the three tested enzymes than β-lactoglobulin hydrolysate. Especially high biological activities were exhibited by peptide fractions of molecular weight lower than 3 kDa, with ACE IC50 <0.64 mg/mL and DPP-IV IC50 <0.55 mg/mL. This study suggests that peptides generated from whey proteins may support postprandial glycemia regulation and blood pressure maintenance, and could be used as functional food ingredients in the diet of patients with type 2 diabetes.     

Conversion of acid hydrolysate of oil palm empty fruit bunch to L-lactic acid by newly isolated Bacillus coagulans JI12

Cost-effective conversion of lignocellulose hydrolysate to optically pure lactic acid is commercially attractive but very challenging. Bacillus coagulans JI12 was isolated from natural environment and used to produce L-lactic acid (optical purity?>?99.5 %) from lignocellulose sugars and acid hydrolysate of oil palm empty fruit bunch (EFB) at 50 °C and pH 6.0 without sterilization of the medium. In fed-batch fermentation with 85 g/L initial xylose and 55 g/L xylose added after 7.5 h, 137.5 g/L lactic acid was produced with a yield of 98 % and a productivity of 4.4 g/L?h. In batch fermentation of a sugar mixture containing 8.5 % xylose, 1 % glucose, and 1 % L-arabinose, the lactic acid yield and productivity reached 98 % and 4.8 g/L?h, respectively. When EFB hydrolysate was used, 59.2 g/L of lactic acid was produced within 9.5 h at a yield of 97 % and a productivity of 6.2 g/L?h, which are the highest among those ever reported from lignocellulose hydrolysates. These results indicate that B. coagulans JI12 is a promising strain for industrial production of L-lactic acid from lignocellulose hydrolysate.     

Isosorbide-based peptidomimetics as inhibitors of hepatitis C virus serine protease

Hepatitis C infection is a cause of chronic liver diseases such as cirrhosis and carcinoma. The current therapy for hepatitis C has limited efficacy and low tolerance. The HCV encodes a serine protease which is critical for viral replication, and few protease inhibitors are currently on the market. In this paper, we describe the synthesis and screening of novel isosorbide-based peptidomimetic inhibitors, in which the compounds 1d, 1e, and 1i showed significant inhibition of the protease activity in vitro at 100 µM. The compound 1e also showed dose-response (IC₅₀ = 36 ± 3 µM) and inhibited the protease mutants D168A and V170A at 100 µM, indicating it as a promising inhibitor of the HCV NS3/4A protease. Our molecular modeling studies suggest that the activity of 1e is associated with a change in the interactions of S2 and S4 subsites, since that the increased flexibility favors a decrease in activity against D168A, whereas the appearance of a hydrophobic cavity in the S4 subsite increase the inhibition against V170A strain.     

Novel Angiotensin I-Converting Enzyme Inhibitory Peptides Found in a Thermolysin-Treated Elastin with Antihypertensive Activity

Angiotensin I-converting enzyme (ACE) inhibitory activity was generated from elastin and collagen by hydrolyzing with thermolysin. The IC₅₀ value of 531.6 µg/mL for ACE inhibition by the elastin hydrolysate was five times less than 2885.1 µg/mL by the collagen hydrolysate. We confirmed the antihypertensive activity of the elastin hydrolysate in vivo by feeding spontaneously hypertensive rats (male) on a diet containing 1% of the elastin hydrolysate for 9 weeks. About 4 week later, the systolic blood pressure of the rats in the elastin hydrolysate group had become significantly lower than that of the control group. We identified novel ACE inhibitory peptides, VGHyp, VVPG and VYPGG, in the elastin hydrolysate by using a protein sequencer and quadrupole linear ion trap (QIT)-LC/MS/MS. VYPGG had the highest IC₅₀ value of 244 µM against ACE and may have potential use as a functional food.     

A peptide from corn gluten hydrolysate that is inhibitory toward angiotensin I converting enzyme

A peptide (F ₄) that inhibits angiotensin I converting enzyme (ACE) was isolated from corn gluten hydrolysate prepared with Pescalase, a serine protease from Bacillus licheniformis. The N-terminal amino acid sequence of F ₄ was Pro-Ser-Gly-Gln-Tyr-Tyr, having the IC₅₀ value of 0.1 mM. The peptide (F ₄), at 30 mg kg^–1 body weight of rat, antagonized the rat's pressor response to angiotensin I.