Substrate specificity of the serine proteinase from Bacillus subtilis, strain 72

A comparative study of the hydrolysis of various p-nitroanilide substrates (Z-A2-A1-pNA, Z-A3-A2-A1-pNA, and Z-A4-A3-A2-A1-pNA, where A1-An are various amino acid residues, Z is the benzoyloxycarbonylic group and pNA is the p-nitroanilide group), catalyzed by serine proteinase from Bacillus subtilis strain 72, was carried out. It was found that depending on the substrate structure, the hydrolysis may involve both the peptide-p-nitroaniline and the amino acid-amino acid bonds. A kinetic analysis of substrate hydrolysis occurring simultaneously at these two bonds was carried out. The physico-chemical meaning of the kinetic parameters of the given scheme was determined. The quantitative estimation of the enzyme specificity with respect to both hydrolyzing bonds can be found by using the parameters calculated during the analysis of the kinetic curve of p-nitroaniline production. It was found that according to their specificity the amino acid residues at position A1 can be arranged in the following order: L-Leu greater than P-Phe greater than L-Ile greater than L-Ala. The beta-branched amino acid residues, L-Val and L-Ile, do not bind to subsite S1. If these residues occupy position A1, the substrate splitting occurs exclusively between residues A1 and A2. The tetrapeptide N-protected p-nitroanilide substrates are also hydrolyzed at this bond. Partial hydrolysis of the amino acid-amino acid bond between residues A1 and A2 occurs in two cases: i) when residue A1 is loosely bound to subsite S1 and/or, ii) when residue A2 is firmly bound to subsite S1.     

A new approach for sample preparation of protein hydrolyzates for amino acid analysis

Sample preparations of protein hydrolyzates for amino acid analysis by ion-exchange chromatography has been accomplished without the removal of hydrochloric acid which was used for the hydrolysis. The technique involves partial neutralization of the available hydrochloric acid after hydrolysis with a solution which neutralizes and dilutes the sample hydrolyzate at the same time. The resulting sample solution which is employed for amino acid analysis produces an amino acid chromatogram having the same elution times and resolution as compared to a mixture of amino acids prepared in pH 2.2 sodium citrate buffer. Experimental data is also presented which shows that the amount of available hydrochloric acid in the final sample solution employed for amino acid analysis can affect both the resolution and elution time of many of the amino acids found in a protein hydrolyzate.     

Lime treatment of keratinous materials for the generation of highly digestible animal feed: 2. Animal hair

Air-dried cow hair was treated using Ca(OH)(2) (insoluble in water but dissolved during reaction) at 100 degrees C. To obtain a liquid product rich in amino acids, a well-insulated, stirred reactor was used to perform the hydrolysis process for different time periods. High lime loadings and a long treatment period convert 70% of cow hair to soluble amino acids and polypeptides. Protein solubilization varies with lime loading especially for the long-term treatment (t>12h) showing that the hydroxyl group is required as a catalyst for the hydrolysis reaction and that lime is consumed during the process; as a consequence lower lime loading generate lower conversions. A very perceptible ammonia odor in the soluble product suggests amino acid degradation. Arginine, threonine, and serine are the more susceptible amino acids under alkaline hydrolysis. The amino acid composition of the solubilized product compares poorly with the essential amino acid requirements for various monogastric domestic animals, but it has value as ruminant feed.     

Gas chromatographic analysis of amino acid enantiomers in Carbetocin peptide hydrolysates after fast derivatization with pentafluoropropyl chloroformate

A novel sample preparation protocol for gas chromatographic (GC) analysis of amino acid enantiomers in peptides was developed. It comprises traditional acid hydrolysis, a novel treatment of the analytes with a fluoroalkyl chloroformate and GC/FID separation of enantiomers on a chiral capillary column. The major improvements consist in that the derivatization step proceeds in organic-aqueous media within seconds and the amino acid derivatives are volatile enough to suit the temperature range of the chiral Chirasil-Val capillary column. The approach was found beneficial for chiral analysis of pharmaceutically important Carbetocin peptide.     

Optimization of enzymatic hydrolysis of visceral waste proteins of Catla (Catla catla) for preparing protein hydrolysate using a commercial protease

Protein hydrolysate was prepared from visceral waste proteins of Catla (Catla catla), an Indian freshwater major carp. Hydrolysis conditions (viz., time, temperature, pH and enzyme to substrate level) for preparing protein hydrolysates from the fish visceral waste proteins were optimized by response surface methodology (RSM) using a factorial design. Model equation was proposed with regard to the effect of time, temperature, pH and enzyme to substrate level. An enzyme to substrate level of 1.5% (v/w), pH 8.5, temperature of 50 degrees C and a hydrolysis time of 135 min were found to be the optimum conditions to obtain a higher degree of hydrolysis close to 50% using alcalase. The amino acid composition of the protein hydrolysate prepared using the optimized conditions revealed that the protein hydrolysate was similar to FAO/WHO reference protein. The chemical scores computed indicated methionine to be the most limiting amino acid. The protein hydrolysate can well be used to meet the amino acid requirements of juvenile common carp and hence has the potential for application as an ingredient in balanced fish diets.     

Kinetics of amino acid production from bean dregs by hydrolysis in sub-critical water

Amino acids play an important physiological role in all life-forms and can be recovered from bean dregs waste using sub-critical water hydrolysis. This work deals with the hydrolysis kinetics of bean dregs. Kinetics was conducted in a temperature range of 200–240°C using a 300-ml stainless steel batch reactor. Since the reaction kinetics in sub-critical water is very complicated, a simplified kinetic model to describe the hydrolysis of bean dregs is proposed: a single consecutive reaction. The differential equations resulting from the model were fit to experimental data to obtain kinetic rate constants. By means of the Arrhenius plot, the activation energy as well as the pre-exponential factor was determined. A good agreement between the simplified model and the experimental data was obtained. The kinetic parameters provided useful information for understanding the hydrolysis reaction of bean dregs. The experimental results show that the best hydrolysis technology is: reaction temperature 200°C, reaction time 20 min. Under this condition, the total amino acid yield reaches 52.9%. Based on the results, this method could become an efficient method for bean dregs liquefaction, producing valuable amino acid.     

A method for chromatographic separation and fluorometric quantification of 2'',3''-cyclic nucleotide-3''-phosphodiesterase reaction products

Treatment of hydrochloric acid with sodium sulfite prior to the acid hydrolysis of bovine pancreatic ribonuclease A has been found to suppress the oxidation of cystine, methionine, and tyrosine without adversely affecting the recoveries of other amino acids. Statistical analysis of the results indicated that the assumption of the independence of the mean and the variance, an assumption commonly used in the evaluation of the effects of various treatments, may not be valid in evaluating antioxidants used in the acid hydrolysis of proteins.     

Hydrolysis of proteins and peptides in a hermetically sealed microcapillary tube: high recovery of labile amino acids

A method for the hydrolysis of peptides and proteins in a hermetically sealed microcapillary tube has been developed. The method is based on the concept that oxidative degradation of labile amino acids during acid hydrolysis of proteins and peptides at high temperature can be reduced to a minimum by limiting the ratio of air to liquid (v/v, less than 1:10) in a microcapillary tube. Furthermore, the physical constraints imposed by the capillary tube will restrict the exposure of the protein solution to air at a very limited area at the meniscus of the liquid. This method eliminates the necessity of time-consuming sealing under vacuum and/or flushing with nitrogen to remove oxygen in the hydrolysis tube. High recovery of labile amino acids can be obtained in a reproducible manner. Because of the simplicity and high reproducibility of the method described, it could be the method of choice for the hydrolysis of protein and peptide intended for quantitative amino acid analysis. Performic acid oxidation is performed at 50 degrees C for 10 min instead of 4 to 20 h at 0 degrees C to achieve an equally good yield of cysteic acid and methionine sulfone from peptides and proteins.     

The destruction of serine and threonine thiohydantoins during the sequence determination of peptides by 4-N,N-dimethylaminoazobenzene 4'-isothiocyanate.

1. A mechanism for the destruction of serine and threonine thiohydantoins during protein sequence analysis by the Edman-type degradation is proposed. The mechanism begins with the dehydration of serine and threonine side chains (at the cyclization stage) which occurs mainly in anhydrous acid solution. The dehydrated derivatives finally polymerize by way of the reactive methylene group (enamine) to form polymers with various molecular weights. In aqueous acid solution, the dehydrated thiohydantoins of serine and threonine undergo hydration (according to the Markovnikov rule) and ring fission, which leads to the irreversible breakdown of thiohydantoin ring. The serine derivative shows a much greater tendency to undergo these side-reactions than the threonine derivative. 2. In the presence of oxygen, the alkaline hydrolysis of amino acid thiohydantoins goes through an oxidation-deamination reaction at the C-N bond of the thiohydantoin ring and leads to the formation of thiourea derivative and keto acids. This reaction mechanism accounts for the low recoveries of amino acid obtained from the alkaline hydrolysis of amino acid thiohydantoins.     

Plant protein hydrolysates as fish fry feed in aquaculture. Hydrolysis of rapeseed proteins by an enzyme complex from king crab hepatopancreas

Rapeseed proteins were processed by an enzyme complex isolated from king crab hepatopancreas in order to obtain a hydrolysate for use as fish fry feed. The amino acid composition of the obtained protein preparation was close to the amino acid composition of fishmeal traditionally used in the production of fish feed. SDS-PAGE, HPLC, and mass spectrometric analysis of the products of enzymatic hydrolysis of rapeseed proteins showed that the proteins were hydrolyzed to a high degree. The composition of the hydrolysates depended on the hydrolysis time and included free amino acids (27% of the total weight of the protein mix after 3 h of hydrolysis and 56% after 21 h of hydrolysis), short peptides (2 to 20 amino acid residues), and small amounts of protein fragments with a molecular weight of approximately 14 kDa, as shown by by SDS-PAG electrophoresis.     

Hydrolysis technology of biomass waste to produce amino acids in sub-critical water

Hydrolysis of biomass waste (such as fish waste, chicken waste, hair and feather) to produce amino acids was studied in sub-critical water, with reaction temperatures from 180 to 320 degrees C and reaction pressures from 3 to 30 MPa. The product of amino acid was determined by Amino Acid Analyzer (BioLC), and 18 kinds of amino acid were obtained. The results show that the controlling of reaction atmosphere, pressure, temperature and time of hydrolysis is very important to obtain high yield of amino acid; most of amino acids reached maximum yield at reaction temperature range of 200-290 degrees C and reaction time range of 5-20 min. There are obvious changes of amino acids yield at reaction pressures of 6-16 MPa and reaction temperature around 260 degrees C, owing to the homogeneousness of the first two phases of water in the formation of vapor and liquid. There are different yields of the same amino acid in different reaction atmospheres (e.g. air, carbon dioxide and nitrogen).     

Acid hydrolysis of protein in a microcapillary tube for the recovery of tryptophan

The acid hydrolysis of proteins was miniaturized and simplified by employing microcapillary tubes (100 microl in volume) with 6 M HCl containing 1% 2-mercaptoethanol and 3% phenol for an amino acid compositional analysis. The method not only eliminated the laborious evacuation step for the hydrolysis tube but also decreased the destruction of tryptophan during hydrolysis. The recovery of tryptophan was 79% by acid hydrolysis at 145 degrees C for 4 h. Since the acid mixture could be removed under vacuum, the hydrolysate was subjected to an amino acid analysis without neutralization or dilution.     

Extraction of protein and amino acids from deoiled rice bran by subcritical water hydrolysis

This study investigated the production of value-added protein and amino acids from deoiled rice bran by hydrolysis in subcritical water (SW) in the temperature range between 100 and 220 degrees C for 0-30 min. The results suggested that SW could effectively be used to hydrolyze deoiled rice bran to produce useful protein and amino acids. The amount of protein and amino acids produced are higher than those obtained by conventional alkali hydrolysis. The yields generally increased with increased temperature and hydrolysis time. However, thermal degradation of the product was observed when hydrolysis was carried out at higher temperature for extended period of time. The highest yield of protein and amino acids were 219 +/- 26 and 8.0 +/- 1.6 mg/g of dry bran, and were obtained at 200 degrees C at hydrolysis time of 30 min. Moreover, the product obtained at 200 degrees C after 30 min of hydrolysis exhibited high antioxidant activity and was shown to be suitable for use as culture medium for yeast growth.     

Enzymatic hydrolysis of the Eisenia andrei earthworm: Characterization and evaluation of its properties

Some studies have carried out in order to retrieve proteins from the by-product of animal-processing industries. Earthworms are rich in protein and usually are used in animal feed. Thus, this study aimed to optimize the hydrolysis process of Eisenia andrei earthworms by employing Alcalase enzyme. Using the response surface methodology, we evaluated the following conditions: temperature, hydrolysis time, stirring speed, and enzyme/substrate ratio. The optimal conditions for the experimental design were determined through the analysis of the foaming and emulsifying properties, in vitro starch digestibility, and antioxidant activity. The results demonstrate that the highest degree of hydrolysis (i.e., 92%) was obtained under the following conditions: pH, 9.5; temperature, 25?°C; hydrolysis time, 2.25?h; stirring speed, 200?rpm; and enzyme/substrate ratio, 1.77%, using Alcalase enzyme. Evaluation of the amino acid composition under these conditions revealed higher concentrations of aspartic acid, glutamic acid, and leucine. The in vitro protein digestibility of the hydrolysate was approximately 73%. There were no significant improvements in either foam stability or emulsification after enzymatic hydrolysis. Additional studies on the antioxidant activity are required. This bioproduct could potentially serve as a promising supplementary food product.     

Amino acid and peptide ratio in protein hydrolysates for parenteral feeding

Using the method of amino acid analysis and routine methods of protein biochemistry, the ratio of amino acids and peptides in acid and enzyme protein hydrolyzates was determined. Depending on the production procedure, the hydrolyzates under study contained various amounts of free amino acids and peptides in which the number of amino acid residues varied from 2 to 7. Additional hydrolysis of these preparations by leucine aminopeptidase led to a decrease in the peptide content and to an increase in the amino acid content. This may have a beneficial effect on the quality of protein hydrolyzates.     

Forms of Aspartic Acid in Human Urine

It was found by amino acid analysis before and after acid hydrolysis of human urine that most glutamic and aspartic acid was in bound form, while glycine, glutamic and aspartic acids accounted for about 70% of bound amino acids. Fractions rich in peptides containing aspartic acid were obtained by chromatography on various columns, and 7 peptides containing aspartic acid were isolated from these fractions. It may be inferred from these results and from the literatures that there are numerous oligopeptides containing aspartic acid in human urine.     

二次回归正交旋转组合设计对豆粕氨基酸提取工艺的优化

研究了硫酸水解法提取豆粕中复合氨基酸的工艺条件。在单因素实验的基础上,运用二次回归正交旋转组合设计方法进行了优化,建立回归模型方程并确定最佳工艺条件。结果表明,在液固比25:1、硫酸浓度3.1mol.L-1、提取时间16.0h和提取温度125.0℃的条件下,最佳氨氮得率达59.9mg.g-1。     

鸭毛梗制备复合氨基酸工艺条件的研究

采用正交试验方法 ,研究了鸭毛梗水解制备复合氨基酸的工艺条件 ,结果表明 :温度 /压力是影响氨基酸转化率最主要的因素。鸭毛梗水解制备的复合氨基酸转化率盐酸法最高 (82 .36 % ) ,氢氧化钠法最低 (5 8.4 6 % ) ,硫酸法与盐酸法接近(79.4 4 % )。硫酸法产率较高 ,操作方便 ,环境污染和设备腐蚀均小 ,适合大量生产 ,确定为水解制备复合氨基酸介质 ,其最佳工艺条件为 :水解时间 8.0h ,硫酸浓度 3.0mol·L-1,水解温度 12 5℃。氨基酸分析表明 ,水解液中均含有 18种以上氨基酸。     

Isolation and characterization of N-long chain acyl aminoacylase from Pseudomonas diminuta

N-Long chain acyl aminoacylase II (Enzyme II) catalyzing the hydrolysis of N-long chain acyl amino acids was purified about 2,000-fold from the cell extracts of Pseudomonas diminuta with 1.8% of activity yield. The purified enzyme was homogeneous on polyacrylamide gel electrophoresis and the molecular weight was 220,000. Enzyme II differed from N-long chain acyl aminoacylase I (Enzyme I) in molecular weight, in substrate specificity, and in behavior toward temperature and pH. Enzyme II showed broader substrate specificity than Enzyme I and catalyzed the hydrolysis of lipoamino acids containing various amino acid residues, although Enzyme I was almost specific to the lipoamino acids containing L-glutamate. The extent of hydrolysis by Enzyme II reaction varied depending on the kinds of lipoamino acids and were: 100% for palmitoyl-L-glutamate, 91% for myristoyl-L-glutamate, 85% for lauroyl-L-glutamate, 54% for lauroyl-L-aspartate, 28% for stearoyl-L-glutamate and 17.5% for lauroyl-glycine.