Studies on Pectolytic Enzymes of Molds

Experiments have been made on fractionation of the pectolytic enzymes produced by Coniothyrium diplodiella. It has been observed that 30 to 35% of the polygalacturonase (PG) activity of the pectolytic enzymes of the said microorganism is salted out with ammonium sulfate, and this portion contains cndo-PG I, endo-PG II and pectin esterase (PE) (with a trace of exo-PG). The endo-PG I accounts for 60 to 65% of the total PG activity, and the endo-PG II, 25 to 30%. Both types of endo-PG scarcely act on pectin, and hydrolyze pectic acid to the extent of 65 to 70%.     

Evaluation of filamentous fungi and inducers for the production of endo-polygalacturonase by solid state fermentation

Aspergillus oryzae CCT 3940, Aspergillus awamori NRRL 3112 and a Trichoderma sp.) were compared for their capacity to produce endo-polygalacturonase (endo-PG) in solid state fermentation. Maximum pectinolytic activity was reached in 72 h of growth, the best two fungal strains being A. niger T0005007-2 and A. oryzae CCT 3940. Three types of commercial purified pectin and four of unprocessed pectin (tangerine, orange, Tahiti lime and sweet lime rind) were used to assess the effect of pectin on the production of endo-PG by A. niger T0005007-2. Maximum pectinolytic activity was achieved using 6 and 10% (w/w) of purified pectin as inducer. Depending on the origin of the commercial pectin used as inducer, maximum endo-PG levels varied from 223 to 876 units per gram of dry medium (one endo-PG unit (U) was defined as the quantity of enzyme which caused a reduction in viscosity of 50% in a 1% w/v solution of pectin in 30 min), indicating that care should be taken when choosing this component of the medium. When the crude pectins were used as inducers at the same concentration as purified pectin, maximum endo-PG activities were 250-300 units/g. However, by increasing the amount of Tahiti lime rind to 50% (w/w) maximum endo-PG was 919 U/g, thus opening up the possibility of a low cost medium for endo-PG production.     

Studies on Pectolytic Enzymes of Molds

The clarification of apple juice has been studied using six pectolytic enzymes produced by Coniothyrium diplodiella, endo-PG (polygalacturonase) I, II and III, exo-PG and PE (pectinesterase) I and II. Each of these six enzymes had no effect on the clarification of apple juice when acted alone, whereas mixtures of any one of endo-PGs and PEs were all able to clarify the juice. Mixtures of exo-PG and either of PEs has no effect on the clarification. Clarifying activities of PG-PE mixtures were varied with the kind of endo-PG used in each mixture and not with the kind of PE. Clarifying activity of PG-PE mixture depended on either endo-PG or PE activities when the other was kept constant.

Crude enzyme from the mold and a mixture of the four PGs and PE in the ratio of the crude enzyme had essentially identical effect on apple juice as well as on artificial pectin and pectic acid.     

Influence of pectin and glucose on growth and polygalacturonase production by Aspergillus niger in solid-state cultivation

The solid-state production of endo- and exo-polygalacturonases (PG) by Aspergillus niger was studied in a media containing wheat bran, salts, and different citric pectin and/or glucose concentrations. Kinetic analysis of the process indicated that the formation of PG and the growth of A. niger are associated processes. By increasing citric pectin from 0 to 16% (w/w), the maximum A. niger concentration (X _m) was raised from 94 to 121 mg/g dry medium suggesting that pectin can be used by A. niger as a growth substrate besides its role as an inducer. With 16% (w/w) pectin, 281 U exo-PG/gdm and 152 U endo-PG/gdm were obtained. Otherwise, pectin concentrations from 20 to 30% (w/w) hindered both production and growth. A. niger concentrations of 108–113 mg/gdm were achieved in runs with glucose from 5 to 12% (w/w), whereas at 16 and 20% (w/w) glucose, lower X _m values (ca. 100 mg/gdm) were measured. The addition of glucose to the wheat bran medium, up to 10% (w/w) led to maximum endo-PG titers slightly lower than those found in the absence of glucose. Nevertheless, exo-PG formation in these media was strongly increased and activities over 370 U/gdm were achieved. The results suggest that in experiments with pectin concentrations until 16% (w/w), exo-PG production was repressed by pectin-degradation products although these same substances had favored biomass growth. When glucose concentrations over 10% (w/w) were added to the media, the maximum activities of both enzymes decreased drastically, suggesting that glucose at high concentrations also exerts a repressive effect on PG production.     

An exo-poly-alpha-D-galacturonosidase, PehB, is required for wild-type virulence of Ralstonia solanacearum.

Ralstonia solanacearum, which causes bacterial wilt disease of many plant species, produces several extracellular plant cell wall-degrading enzymes that are suspected virulence factors. These include a previously described endopolygalacturonase (PG), PehA, and two exo-PGs. A gene encoding one of the exo-PGs, pehB, was cloned from R. solanacearum K60. The DNA fragment specifying PehB contained a 2,103-bp open reading frame that encodes a protein of 74.2 kDa with a typical N-terminal signal sequence. The cloned pehB gene product cleaves polygalacturonic acid into digalacturonic acid units. The amino acid sequence of pehB resembles that of pehX, an exo-PG gene from Erwinia chrysanthemi, with 47.2% identity at the amino acid level. PehB also has limited similarity to plant exo-PGs from Zea mays and Arabidopsis thaliana. The chromosomal pehB genes in R. solanacearum wild-type strain K60 and in an endo-PG PehA- strain were replaced with an insertionally inactivated copy of pehB. The resulting mutants were deficient in the production of PehB and of both PehA and PehB, respectively. The pehB mutant was significantly less virulent than the wild-type strain in eggplant virulence assays using a soil inoculation method. However, the pehA mutant was even less virulent, and the pehA pehB double mutant was the least virulent of all. These results suggest that PehB is required for a wild-type level of virulence in R. solanacearum although its individual role in wilt disease development may be minor. Together with endo-PG PehA, however, PehB contributes substantially to the virulence of R. solanacearum.     

商品果胶酶中endo－PG的分离纯化及其部分性质研究

以Ａ．ｎｉｇｅｒ来源的果胶酶为材料,经过ＣＭ－ＳｅｐｈａｄｅｘＣ－５０及ＳｅｐｈａｄｅｘＧ－１００两步骤分离纯化得到电泳均一的ｅｎｄｏ－ＰＧ１及ｅｎｄｏ－ＰＧ２,其亚基分子量分别为３５ｋＤ及３７ｋＤ,含糖量为１１．２２％及８．３％,最大紫外吸收峰分别在２７４ｎｍ及２６９ｎｍ处,氨基酸组成分析结果表明Ｇｌｙ含量较高,Ｍｅｔ含量较低,不含Ｃｙｓ,并且酸性氨基酸含量高于碱性氨基酸,圆二色谱结果表明二级结构主要为α螺旋和β折叠,其中ｅｎｄｏ－ＰＧ１含α螺旋４５．１％,β折叠２４．９％;ｅｎｄｏ－ＰＧ２含α螺旋３９．６％,β折叠３６．５％。     

Pectinolytic enzyme production by Bacillus species and their potential application on juice extraction

Five Bacillus strains isolated from decaying vegetable material were cultivated on wheat bran and endo-polygalacturonases, exo-polygalacturonase and pectin lyase activities in the crude enzymatic solution obtained were determined. Highest activity was observed for all enzymes when fermentation was carried out at 28 °C, the highest activity values were obtained after 120 h of cultivation for exo-PG and after 48 h for endo-PG and PL. The use of the enzymatic solution for treatment of fruits and vegetable mash afforded a high juice extraction and a pulp with good pressing characteristics.     

A novel and cost-effective methodology for enhanced production of industrially valuable alkaline xylano-pectinolytic enzymes cocktail in short solid-state fermentation cycle

The aim of this study was to enhance the production of xylano-pectinolytic enzymes concurrently and also to reduce the fermentation period. In this study, the effect of agro-residues extract-based inoculum on yield and fermentation time of xylano-pectinolytic enzymes was studied. Microbial inoculum and fermentation media were supplemented with xylan and pectin polysaccharides derived from agro-based residues. Enzymes production parameters were optimized through two-stage statistical design approach. Under optimized conditions (temperature 37°C, pH 7.2, K₂HPO₄ 0.22%, MgSO₄ 0.1%, gram flour 5.6%, substrate: moisture ratio 1:2, inoculum size 20%, agro-based crude xylan in production media 0.45%, and agro-based crude xylan–pectin in inoculum 0.13%), nearly 28,255 ± 565 and 9,202 ± 193 IU of xylanase and pectinase, respectively, were obtained per gram of substrate in a time interval of 6 days only. The yield of both xylano-pectinolytic enzymes was enhanced along with a reduction of nearly 24 h in fermentation time in comparison with control, using polysaccharides extracted from agro-residues. The activity of different types of pectinase enzymes such as exo-polymethylgalacturonase (exo-PMG), endo-PMG, exo-polygalacturonase (exo-PG), endo-PG, pectin lyase, pectate lyase, and pectin esterase was obtained as 1,601, 12.13, 5637, 24.86, 118.62, 124.32, and 12.56 IU/g, respectively, and was nearly twofold higher than obtained for all seven types in control samples. This is the first report mentioning the methodology for enhanced production of xylano-pectinolytic enzymes in short solid-state fermentation cycle using agro-residues extract-based inoculum and production media.     

Endo-polygalacturonase production from untreated lemon peel byAspergillus sp. CH-Y-1043

Summary Endo-polygalacturonase (endo-PG) production byAspergillus sp. CH-Y-1043 using untreated lemon peel as the sole carbon source was investigated. This strain was observed to produce more activity of endo-PG at 37°C than at 29°C. Untreated lemon peel proved to be a beeter substrate than citrus pectin for endo-PG production. Modification of the culture medium and lowering of the initial pH to 2.8 caused a 10-fold increase in the production of endo-PG activity using lemon peel.     

Utilization of orange peel,a food industrial waste,in the production of exo-polygalacturonase by pellet forming <Emphasis Type="Italic">Aspergillus sojae</Emphasis>

The production of exo-polygalacturonase (exo-PG) from orange peel (OP), a food industrial waste, using Aspergillus sojae was studied in submerged culture. A simple, low-cost, industrially significant medium formulation, composed of only OP and (NH₄)₂SO₄ (AS) was developed. At an inoculum size of 2.8 × 10³ spores/mL, growth was in the form of pellets, which provided better mixing of the culture broth and higher exo-PG activity. These pellets were successfully used as an inoculum for bioreactors and 173.0 U/mL exo-PG was produced. Fed-batch cultivation further enhanced the exo-PG activity to 244.0 U/mL in 127.5 h. The final morphology in the form of pellets is significant to industrial fermentation easing the subsequent downstream processing. Furthermore, the low pH trend obtained during this fermentation serves an advantage to fungal fermentations prone to contamination problems. As a result, an economical exo-PG production process was defined utilizing a food industrial by-product and producing high amount of enzyme.     

Pectinolytic activity of bacteria isolated from soil and two fungal strains during submerged fermentation

Seven different strains were selected for their ability to degrade citrus pectin. Alkaline pectinases were produced by five bacterial soil isolates, whereas two fungal strains produced pectinase in an acidic environment. The bacteria were isolated from soil of a plum orchard in Northern Ireland. These isolates produced significant amounts of pectin lyase (PL) and polygalacturonase (PG) with maximum activities of 30.1 and 29.1 U/ml respectively. Fungal strains Aspergillus sp. and PN-1 produced four different pectinolytic activities; endo-PG, exo-PG, pectin esterase (PE) and PL. The Aspergillus sp. produced higher amounts of pectinase than PN-1. The Aspergillus sp. excreted highly stable pectinases, which may be of importance for industrial applications.     

Quantification of the amount of galacturonic acid residues in blocksequences in pectin homogalacturonan by enzymatic fingerprinting with exo- and endo-polygalacturonase II from Aspergillus niger

A method to determine the amount of galacturonic acid in blocksequence (BS) in pectin homogalacturonan (HG) is described. The method is based on a combination of endopolygalacturonase II (endo-PG II) and exopolygalacturonase (exo-PG) digestion followed by quantification of the liberated galacturonic acid monomer. The amount of monomers released is directly related to the amount of non-esterified galacturonic acid units located between two other non-esterified galacturonic acids units on the HG chain. The amount released for exo-PG digestion only corresponds to the BS located at the non-reducing end of the polymer. The difference between total- and exo-BS was calculated to be the amount of endo-BS located either within or on the reducing end of the HG. Three series of model pectins obtained by de-esterification of a high-ester pectin with either plant pectin methyl-esterase (p-PME, P-series), fungal pectin methyl-esterase (f-PME, F-series) and chemical de-esterification using base (B-series) were analysed and compared with a fully de-esterified pectic acid sample obtained from the same raw material. Clear differences for the increase of the amounts of blocksequence could be seen between de-esterification of the P- and F-series samples supporting a blockwise and a homogenous de-esterification mechanism, respectively. f-PME and base treatment showed only minor differences in the increase of galacturonic acid units in BS, despite differences seen in their methyl-esterification pattern. Differences between the amounts of galacturonic acid located in exo- and endo-BS, provided evidence for the need of a certain start side or blocklength for p-PME to de-esterify blockwise.     

Purification and characterisation of two exo-polygalacturonases from Aspergillus niger able to degrade xylogalacturonan and acetylated homogalacturonan

Two exo-polygalacturonases (EC 3.2.1.67) were purified from a commercial Aspergillus niger enzyme preparation by ammonium sulfate precipitation, preparative electrofocusing, anion-exchange and size-exclusion chromatographies. The enzymes had molar masses of 82 kDa (exo-PG1) and 56 kDa (exo-PG2). Exo-PG1 was stable over wider pH and temperature ranges than exo-PG2. Addition of 0.01 mM HgCl(2) increased the exo-PG2 activity 3.4 times but did not affect exo-PG1. Analysis of the reaction products of (reduced) pentagalacturonate by high-performance anion-exchange chromatography revealed that both enzymes split the substrate from the non-reducing end in a multi-chain attack mode. Exo-PG1 had a broad specificity towards oligogalacturonates with different degrees of polymerisation, while digalacturonate was the most favorable substrate for exo-PG2. Both enzymes degraded xylogalacturonan from pea hull in an exo manner to produce galacturonic acid and Xyl-GalA disaccharide, as identified by electrospray ionization-ion trap mass spectrometry (ESI-ITMS). Moreover, exo-PGs split acetylated homogalacturonan in an exo manner, producing galacturonic acid and acetylated galacturonic acid, as shown by ESI-ITMS.     

Enhancement of acid amylase production by an isolated Aspergillus awamori

AIMS: Evaluation of the influence of fermentation components on extracellular acid amylase production by an isolated fungal strain Aspergillus awamori. METHODS AND RESULTS: Eight fungal metabolic influential factors, viz. soluble starch, corn steep liquor (CSL), casein, potassium dihydrogen phosphate (KH(2)PO(4)) and magnesium sulfate (MgSO(4) x 7H(2)O), pH, temperature and inoculum level were selected to optimize amylase production by A. awamori using fractional factorial design of Taguchi methodology. Significant improvement in acid amylase enzyme production (48%) was achieved. The optimized medium composition consisted of soluble starch--3%; CSL--0.5%; KH(2)PO(4)--0.125%; MgSO(4) x 7H(2)O--0.125%; casein--1.5% at pH 4.0 and temperature at 31 degrees C. CONCLUSION: Optimization of the components of the fermentation medium was carried out using fractional factorial design of Taguchi's L-18 orthogonal array. Based on the influence of interaction components of fermentation, these could be classified as the least significant and the most significant at individual and interaction levels. Least significant factors of individual level have higher interaction severity index and vice versa at enzyme production in this fungal strain. The pH of the medium and substrate (soluble starch) showed maximum production impact (60%) at optimized environment. Temperature and CSL were the least influential factors for acid amylase production. SIGNIFICANCE AND IMPACT OF THE STUDY: Acid amylase production by isolated A. awamori is influenced by the interaction of fermentation factors with fungal metabolism at individual and interaction levels. The pH of the fermentation medium and substrate concentration regulates maximum enzyme production process in this fungal strain.     

Increase in Cell Wall-Associated Phosphatase Activity in Cucumber Roots during Calcium Starvation: Binding Nature and Properties of the Phosphatase and Cell Wall Analysis

In Ca^2$-starved cucumber roots, about 23% of phosphatase assayedat pH 9.0 (ALPase) in the crude cell walls was solubilized witheither 2 M NaCl or purified endo type polygalacturonase (endo-PG)from yeast culture broth. Coexistence of NaCl and endo-PG hadlittle effect on further release of ALPase, and a small amountof the activity was solubilized from the NaCl-pretreated cellwalls by incubation with endo-PG. Ionically bound ALPase, therefore,seemed to be localized in the fraction which was hydrolyzedby endo-PG in the crude cell walls of Ca^2$-starved cucumberroots. In the control roots, however, ALPase was not effectivelysolubilized by the treatment with endoPG. Ca^2$ starvation reducedthe contents of rhamnose, uronic acids and galactose among non-cellulosicsugars in the cell walls, suggesting that the structure of pecticsubstances, possibly rhamnogalacturonan, is altered during thestarvation. Activities of both ionically and covalently bound ALPases greatlyincreased during Ca^2$ starvation. The increased ALPase in theNaCl-solubilized fraction hydrolyzed most phosphate esters tested,whereas the enzyme from control roots only cleaved nucleoside2'(3')-monophosphates and p-nitrophenylphosphate. Differencesin the properties between both types of roots were also foundwhen the effects of various inhibitors were tested. Profilesof ALPase-isozymes after polyacrylamide gel electrophoresiswere also altered by Ca^2$ starvation. (Received June 2, 1982; Accepted July 20, 1982)     

Comparison of stirred tank and airlift bioreactors in the production of polygalacturonases by Aspergillus oryzae

The production of endo and exo-polygalacturonase (PG) by Aspergillus oryzae IPT 301 was studied in a stirred tank bioreactor (STR) and an internal circulation airlift bioreactor. Using a factorial experimental design, a soluble culture medium was defined which allowed the production of exo- and endo-PG comparable to that obtained in a medium containing suspended wheat bran. The soluble medium was used in tests to compare the production of these enzymes in the STR and airlift bioreactor. In these tests, after 96 h, maximum enzymatic activity values achieved for exo- and endo-PG were 65.2 units (U) per mL and 91.3 U mL⁻¹, in the STR, with similar activity values of 60.6 U mL⁻¹ and 86.2 U mL⁻¹, respectively, being achieved in the airlift bioreactor. The airlift bioreactor also showed satisfactory results regarding the oxygen transfer rate in this process, indicating its potential to be used in an eventual larger scale production of exo- and endo-PG, with lower costs for both installation and operation.     

Endo-PG诱导培养小麦细胞PGIP产生的研究

内切多聚半乳糖醛酸酶（endo-polygalacturonase,endo-PG）是待异水解细胞壁成分多聚半乳糖醛酸的酶,水解产生的10～13个糖基的寡聚半乳糖醛酸片段是活性诱导因子,激活植物自身防御系统．我们已研究发现单子叶植物小麦中存在多聚半乳糖醛酸酶抑制蛋白（polygalacturonaseinhibitingprotein,PGIP）,并已将其分离纯化,对其性质作了初步研究[1,2]文献报导[3]PGIP是在未分化的细胞中合成的．本文报导在悬浮培养的小麦细胞中加入Endo-PG观察其PGIP的生成,比较赤霉病的高抗品种与低抗品种中PGIP的合成情况,探讨PGIP与植物防御作…     

Expression and Characterization of Fifteen <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> 99-880 Polygalacturonase Enzymes in <Emphasis Type="Italic">Pichia pastoris</Emphasis>

Polygalacturonase (PG) enzymes hydrolyze the long polygalacturonic acid chains found in the smooth regions of pectin. Interest in this enzyme class continues due to their ability to macerate tissues of economically important crops and their use in a number of industrial processes. Rhizopus oryzae has a large PG gene family with 15 of 18 genes encoding unique active enzymes. The PG enzymes, 12 endo-PG and 3 exo-galacturonases, were expressed in Pichia pastoris and purified enabling biochemical characterization to gain insight into the maintenance of this large gene family within the Rhizopus genome. The 15 PG enzymes have a pH optima ranging from 4.0 to 5.0. Temperature optima of the 15 PG enzymes vary from 30 to 40°C. While the pH and temperature optima do little to separate the enzymes, the specific activity of the enzymes is highly variable ranging from over 200 to less than 1 μmol/min/mg. A general pattern related to the groupings found in the phylogentic tree was visible with the group containing the exo-PG enzymes demonstrating the lowest specific activity. Finally, the progress curves of the PG enzymes, contained within the phylogenetic group that includes the exo-PG enzymes, acting on trigalacturonic acid lend additional support to the idea that the ancestral form of PG in Rhizopus is endolytic and exolytic function evolved later.     

Ethanol production from starch by a coimmobilized mixed culture system of Aspergillus awamori and Saccharomyces cerevisiae

The development of a coimmobilized mixed culture sys tem of aerobic and facultative anaerobic microorganisms in Ca-alginate gel beads and the production of useful metabolites by the system were investigated. A coimmobilized mixed culture system of Aspergillus awamori (obligate aerobe) and Saccharomyces cerevisiae (facultative anaerobe) in Ca-alginate gel beads was used as a model system, and ethanol production from starch by the system was used as a model production. Mold Asp. awamori is an amylolytic microorganism while yeast S. cerevisiae is an ethanol producer. The two microorganisms grew competitively in the oxygen-rich surface area of the gel beads because they had similar oxygen demands in aerobic culture conditions. Neither microorganism exhibited "habitat segregation" in the gel beads and leaked yeast cells grew aerobically without ethanol production in the broth. Ethanol productivity was low under these conditions.A more desirable coimmobilized mixed culture system of Asp. awamori and S. cerevisiae was established by adding Vantocil IB (a biocidal compound) to the production medium. The antimicrobial activity of Vantocil IB was more effective with S. cerevisiae than with Asp. awamori, so that a dense mycelial layer of Asp. awamori formed in the surface of the gel beads While S. cerevisiae grew densely in the more inner areas of the gel beads. Also, yeast cell leakace was repressed and ethanol productivity was improved. The system with Vantocil IB produced ethanol of 4.5 and 12.3 g/L from 16 and 40 g/L starch, respectively. A continuous culture using this system with Vantocil IB was also carried out, and a stable steady state could be maintained for six days without leakage of yeast cells and contamination. The selection of a factor suitable for producing "habitat segregation" enabled the development of a coimmobilized mixed culture system of an aerobe and a facultative anaerobe. In this study, total habitat segregation was used to denote a tendency to exhibit denser growth in different parts of one gel bead.