A factorial design analysis of chitin production by Cunninghamella elegans

Chitin production by Cunninghamella elegans (IFM 46109) was studied with a two-level full factorial design, varying time of cultivation and the concentration of D-glucose, L-asparagine, and thiamine in the culture medium. The material extracted was characterized by infrared and NMR spectroscopy. The highest chitin yield, 28.8%, was comparable with the highest in the literature and was obtained with a medium containing 60 g.L-1 of glucose, 3 g.L-1 of asparagine, and 0.008 mg.L-1 of thiamine. Increasing the time of cultivation from 24 h to 72 h did not affect chitin production. The three factors showed significant positive effects on chitin production, without interactions between them.     

响应面法优化毛霉菌发酵培养基

采用响应面分析方法优化毛霉菌B的发酵培养基,首先通过单因素试验筛选出葡萄糖为最适碳源,酵母膏和玉米浆为最适氮源,用Plackett—Burman试验对葡萄糖、酵母膏、玉米浆、MgSO4、FeSO4、NILCl/、HPO4进行评估并筛选出具有显著效应的3个因素：葡萄糖、酵母膏、玉米浆,再通过最陡爬坡试验逼近其最大响应区域,最后采用Box—Behnken试验对其用量进行优化,得到毛霉菌最佳发酵培养基（g/L）：葡萄糖51．54,酵母膏5．22,玉米浆14．31,MgSO40．5,FeSO40．1,NH4Cl3,k2HPO43,pH6．0～6．5。培养基优化后,毛霉生物量由23．51g／L提高至31．13g/L,比对照组提高32．41％,腺嘌呤转化率由53．59％提高至59．97％,ATP产率由6．56g／L提高至7．34g／L,比对照组提高11．89％。     

Properties of chitin synthetase in isolated chitosomes from yeast cells of Mucor rouxii.

Chitin synthetase was isolated and purified 120-fold from the supernatant fraction (54,500 X g) of broken yeast cells of Mucor rouxii. The purified preparations consisted mainly of chitin synthetase particles (chitosomes) with an average size larger than 7 X 10(6) daltons (by gel filtration) and an average sedimentation coefficient of 105 S. The samples also contained other enzyme complexes (fatty acid synthetase, pyruvate dehydrogenase, and, depending on method, ribosomes). Nearly all of the chitosomal chitin synthetase occurred in a zymogenic form that required proteolytic activation. In most properties, the chitosomal enzyme was similar to crude enzyme (54,000 X g sediment): kinetics, activation by proteases, response to metals, stimulation by N-acetylglucosamine, and inhibition by polyoxin or UDP. One mamor difference was the much greater stability of the chitosomal chitin synthetase zymogen against spontaneous activation and destruction. Product (chitin microfibril) and enzyme (chitin synthetase) remained associated in a complex that was readily separated by centrifugation.     

Production of phytase by Mucor racemosus in solid-state fermentation

Phytase production was studied by three Mucor and eight Rhizopus strains by solid-state fermentation (SSF) on three commonly used natural feed ingredients (canola meal, coconut oil cake, wheat bran). Mucor racemosus NRRL 1994 (ATCC 46129) gave the highest yield (14.5 IU/g dry matter phytase activity) on coconut oil cake. Optimizing the supplementation of coconut oil cake with glucose, casein and (NH(4))(2)SO(4), phytase production in solid-state fermentation was increased to 26 IU/g dry matter (DM). Optimization was carried out by Plackett-Burman and central composite experimental designs. Using the optimized medium phytase, alpha-amylase and lipase production of Mucor racemosus NRRL 1994 was compared in solid-state fermentation and in shake flask (SF) fermentation. SSF yielded higher phytase activity than did SF based on mass of initial substrate. Because this particular isolate is a food-grade fungus that has been used for sufu fermentation in China, the whole SSF material (crude enzyme, in situ enzyme) may be used directly in animal feed rations with enhanced cost efficiency.     

A pathway of chitosan formation in Mucor rouxii. Enzymatic deacetylation of chitin.

1. An enzyme that catalyzes hydrolysis of acetamido groups of chitin derivatives was found in the supernatant fraction of Mucor rouxii. 2. Partially O-hydroxyethylated chitin (glycol chitin) was used as a substrate in the purification and characterization of this enzyme. A 140-fold purification was obtained by means of ammonium sulfate fractionation followed by chromatography on carboxymethylcellulose and DEAE-cellulose. 3. The enzyme releases about 30% of the acetyl groups of glycol chitin, giving a product with a decreased sensitivity to lysozyme. The enzyme also deacetylates chitin and N-acetylchitooligoses, whereas it is inactive toward bacterial cell wall peptidoglycan, N-acetylated heparin, a polymer of N-acetylgalactosamine, di-N-acetylchitobiose and monomeric N-acetylglucosamine derivatives. 4. This enzyme shows a pH optimum of 5.5. The Km value for glycol chitin is 0.87 g/l or 2.6 mM with respect to monosaccharide residues. 5. The occurrence of this enzyme accounts for the formation of chitosan in fungi.     

The co-ordination of chitosan and chitin synthesis in Mucor rouxii

Chitin synthetase preparations from cell walls and chitosomes of the fungus Mucor rouxii were tested for their ability to synthesize chitosan when incubated with uridine diphosphate N-acetyl-D-glucosamine in the presence of chitin deacetylase. The most effective chitin synthetase preparation was one dissociated from cell walls with digitonin. The rate of chitosan synthesis by the wall-dissociated chitin synthetase was about three times that of an equivalent amount of cell walls. The chitosan-synthesizing ability of chitosomes was relatively low, but was more than tripled by treatment with digitonin. Presumably, digitonin improves chitosan yields of dissociating chitin synthetase. The dissociated enzyme would produce dispersed chitin chains that could be attacked by chitin deacetylase before they have time to crystallize into microfibrils. The regulation of chitin and chitosan syntheses in vivo may be determined by the organization of chitin synthetase molecules at the cell surface. Those molecules that remain organized as a complex, similar if not identical to that found in chitosomes, would produce mainly chitin. Chitosan would be preferentially produced by chitin synthetase molecules which are dispersed upon reaching the cell surface.     

Direct ethanol production from N-acetylglucosamine and chitin substrates by Mucor species

Chitin, which is a polymer of β-(1–4) linked N-acetyl-d-glucosamine (GlcNAc) residues, is one of the most abundant renewable resources in nature, after cellulose. In this study, we found some native Mucor strains, which can use GlcNAc and chitin substrates as carbon sources for growth and ethanol production. One of these strains, M. circinelloides NBRC 6746 produced 18.6 ± 0.6 g/l of ethanol from 50 g/l of GlcNAc after 72 h and the maximum ethanol production rate was 0.75 ± 0.1 g/l/h. Furthermore, M. circinelloides NBRC 4572 produced 6.00 ± 0.22 and 0.46 ± 0.04 g/l of ethanol from 50 g/l of colloidal chitin and chitin powder after 16 and 12 days, respectively. We also found an extracellular chitinolytic enzyme producing strain M. ambiguus NBRC 8092, and successfully improved ethanol productivity of NBRC 4572 from colloidal chitin using crude chitinolytic enzyme derived from NBRC 8092. The ethanol titer reached 9.44 ± 0.10 g/l after 16 days. These results were the first bioethanol production from GlcNAc and chitin substrates by native organisms, and also suggest that these Mucor strains have great potential for the simultaneous saccharification and fermentation (SSF) of chitin biomass.     

Production of chitinolytic enzymes by a strain (BM17) of Paenibacillus pabuli isolated from crab shells samples collected in the east sector of central Tyrrhenian Sea

Nineteen bacterial isolates were grown in shaken cultures in media containing chitin as carbon source and different additional nitrogen sources such as yeast nitrogen base (YNB), yeast extract (YE), corn steep liquor (CSL) and ammonium sulfate. Strain BM17 showed the highest activity (200 U/l) in medium containing Chitin (1%) and YNB (0.5%). Molecular analysis of the 16S rRNA gene showed that strain BM17 belongs to the species Paenibacillus pabuli (99.72% homology). The enzyme activity started after 12-24 h; exponential enzyme production was recorded from the 24th h and lasted till the 96th h of incubation when activity peaked to decrease thereafter. Medium optimisation was carried out by Response Surface Methodology (RSM) considering the effects of chitin, corn steep liquor and yeast extract. BM17 chitinolytic activity was induced by chitin but the increase of its concentration did not have significant effects on the enzyme activity. By contrast, the nitrogen source, particularly YE, strongly affected the enzyme production.     

The Production of Pyruvic and {alpha}-Oxoglutaric Acids by Mucor Species

Six out of the seven species of Mucor studied (M. plumbeus,M. racemosus, M. rouxii, M. hiemalis, M. ramannianus, and M.mucedo) are shown to produce pyruvic acid when grown on a mediumcontaining glucose, glutamate, and mineral salts. Mucor pusillusproduces no detectable pyruvate on this medium. The proportionof the carbohydrate metabolized which is excreted as pyruvateis greatest in species having a high thiamine requirement forgrowth. Addition of thiamine to the culture medium reduces pyruvateexcretion. However, in the species which need added thiaminefor growth, the growth requirement is almost completely satisfiedby 20 µg thiamine per litre whereas suppression of pyruvateexcretion requires about 200 µg thiamine per litre. Experimentswith M. plumbeus show that the yield of pyruvate is reducedwhen xylose is substituted for glucose and also when alanineis substituted for glutamate in the medium. -Oxoglutaric acidis produced by all seven species on the glucose/glutamate medium,the yield varying with the species. This acid is partly derivedfrom the glutamate in the medium.     

Synthesis of Acid Protease from Mucor miehei: Integration of Production and Recovery

The production of acid protease from Mucor Miehei was repressed by amino acid additions (3·5-5·0 g/litre) from hydrolysed casein. The integration of the batch bioprocess with an ultrafiltration unit proved effective in depressing enzyme production. A hollow fibre ultrafilter with a 5000 MW cutoff was used to reduce the concentration of amino acids present in the medium after enzyme concentration began to decline. Volume concentrating ratio (VCR) values of 2 and 3 were used for the experiments. Increases as high as 25% in enzyme concentration were achieved.     

Structural characterization of chitin and chitosan obtained by biological and chemical methods

Chitin production was biologically achieved by lactic acid fermentation (LAF) of shrimp waste (Litopenaeus vannameii) in a packed bed column reactor with maximal percentages of demineralization (D(MIN)) and deproteinization (D(PROT)) after 96 h of 92 and 94%, respectively. This procedure also afforded high free astaxanthin recovery with up to 2400 μg per gram of silage. Chitin product was also obtained from the shrimp waste by a chemical method using acid and alkali for comparison. The biologically obtained chitin (BIO-C) showed higher M(w) (1200 kDa) and crystallinity index (I(CR)) (86%) than the chemically extracted chitin (CH-C). A multistep freeze-pump-thaw (FPT) methodology was applied to obtain medium M(w) chitosan (400 kDa) with degree of acetylation (DA) ca. 10% from BIO-C, which was higher than that from CH-C. Additionally, I(CR) values showed the preservation of crystalline chitin structure in BIO-C derivatives at low DA (40-25%). Moreover, the FPT deacetylation of the attained BIO-C produced chitosans with bloc copolymer structure inherited from a coarse chitin crystalline morphology. Therefore, our LAF method combined with FPT proved to be an affective biological method to avoid excessive depolymerization and loss of crystallinity during chitosan production, which offers new perspective applications for this material.     

甲壳质脱乙酰基酶的研究概况及进展

甲壳质脱乙酰基酶（ｃｈｉｔｉｎｄｅａｃｅｔｙｌａｓｅ）最初是从真菌毛霉（Ｍｕｃｏｒ．ｒｏｕｘｉ）分离纯化的一种乙酰基转移酶。这种酶可以催化脱去甲壳质分子中Ｎ－乙酰葡糖胺链上的乙酰基,而使之变成壳多糖［１］。除几种真菌外,在昆虫中也发现了这种酶的存在［２］。真菌的甲壳质脱乙酰基酶主要参与真菌细胞壁的形成［３］,还与真菌自溶的过程中的细胞壁裂解有关［４］。最近又发现它参与植物和病原微生物的相互作...     

Production of Alcaligenes xylosoxydans EMS33 in a Bench-scale Fermenter

Summary Optimization of medium composition and pH for chitinase production by the Alcaligenes xylosoxydans mutant EMS33 was carried out in the present study and the optimized medium composition and conditions were evaluated in a fermenter. The medium components screened initially using Plackett–Burman design were (NH₄)₂SO₄, MgSO₄ 7H₂O, KH₂PO₄, yeast extract, Tween 20 and chitin in shake flask experiments. The significant medium components identified by the Plackett–Burman method were MgSO₄ 7H₂O, Tween 20 and chitin. Central composite response surface methodology was applied to further optimize chitinase production. The optimized values of MgSO₄ 7H₂O, Tween 20, chitin and pH were found to be 0.6 g/l, 0.05 g/l, 11.5 g/l and 8.0, respectively. Chitinase and biomass production of Alcaligenes xylosoxydans EMS33, was studied in a 2-l fermenter containing (g/l): chitin, 11.5; yeast extract, 0.5; (NH₄)₂SO₄, 1; MgSO₄ 7H₂O, 0.6; KH₂PO₄, 1.36 and Tween 20, 0.05. The highest chitinase production was 54 units/ml at 60 h and pH 8.0 when the dissolved O₂ concentration was 60%, whereas the highest biomass production was achieved at 36 h and pH 7.5 without any dissolved O₂ control.     

Ethanol and value‐added byproducts from rice straw by dimorphic fungus Mucor hiemalis

Different morphologies of Mucor hiemalis were induced and used for the production of ethanol and biomass from rice straw through a separate hydrolysis and fermentation process. The yield of enzymatic hydrolysis was improved from 40.4% for the untreated straw to 80–93% by employing sodium hydroxide and concentrated phosphoric acid pretreatments with or without ultrasonication. The best hydrolysis performance was achieved after pretreatment by sodium hydroxide assisted with ultrasonication. The ethanol yields from the hydrolysates were 0.39–0.44 g/g depending on the pretreatment method and the fungus morphology. The yeast‐like form of the fungus showed faster glucose assimilation and slightly higher ethanol yield compared to the other morphologies. The biomass yield of mostly yeast‐like cells was more than the other morphologies (0.202–0.282 g/g glucose). Moreover, the biomass of the yeast‐like cells had more protein content (46.7–52.4 %) compared to filamentous cells (37.7–46.3 %). The cell wall, alkali‐insoluble material (AIM) of the biomass, represented 16.3–20.1% of the biomass. On average, total chitin‐chitosan content of AIM of the biomass of purely filamentous, mostly filamentous, mostly yeast‐like, and purely yeast‐like forms of the fungus was 0.460, 0.373, 0.330, and 0.336 g/g AIM of the biomass, respectively.     

Influence of plant growth hormones on the growth of Mucor rouxii and chitosan production

Supplementation of molasses-salt medium with plant growth hormones, viz., indoleacetic acid, indolebutyric acid, kinetin and gibberellic acid, increased chitosan production by Mucor rouxii as well as its growth at different optimum concentrations. The increase in yield of chitosan was found to range from 34% to 69% and mycelial growth from 12% to 17.4%. Gibberellic acid was the most potent in this respect. Sixty-nine percent more chitosan over the control could be obtained from 1l of the medium supplemented with 3mg gibberellic acid. Degree of acetylation of chitosan ( approximately 13%) was not changed due to addition of hormone in the medium but weight average molecular weight of chitosan increased by more than 50%. Thus, the plant growth hormones add a value to chitosan by increasing its molecular weight.     

Production of ethanol by filamentous and yeast-like forms of <Emphasis Type="Italic">Mucor indicus</Emphasis> from fructose,glucose, sucrose,and molasses

The fungus Mucor indicus is found in this study able to consume glucose and fructose, but not sucrose in fermentation of sugarcane and sugar beet molasses. This might be an advantage in industries which want to selectively remove glucose and fructose for crystallisation of sucrose present in the molasses. On the other hand, the fungus assimilated sucrose after hydrolysis by the enzyme invertase. The fungus efficiently grew on glucose and fructose and produced ethanol in synthetic media or from molasses. The cultivations were carried out aerobically and anaerobically, and manipulated toward filamentous or yeast-like morphology. Ethanol was the major metabolite in all the experiments. The ethanol yield in anaerobic cultivations was between 0.35 and 0.48 g/g sugars consumed, depending on the carbon source and the growth morphology, while a yield of as low as 0.16 g/g was obtained during aerobic cultivation. The yeast-like form of the fungus showed faster ethanol production with an average productivity of 0.90 g/l h from glucose, fructose and inverted sucrose, than the filamentous form with an average productivity of 0.33 g/l h. The biomass of the fungus was also analyzed with respect to alkali-insoluble material (AIM), chitin, and chitosan. The biomass of the fungus contained per g maximum 0.217 g AIM and 0.042 g chitosan in yeast-like cultivation under aerobic conditions.     

The inhibitory protein of chitin synthetase from Mucor rouxii is a chitinase

The 'inhibitor' of chitin synthetase previously isolated from the cytosol of Mucor rouxii was found to be a chitinase. Paper chromatographic analysis of reaction products showed that the overall rate of chitin synthesis was unaffected by the 'inhibitor'. The observed reduction in chitin synthesis was due to depolymerization of chitin, mostly dimers (diacetyl-N,N'chitobiose). The chitinase was much more effective against nascent chitin, i.e., chitin being made in a chitin synthetase incubation mixture, than against preformed chitin.     

Factors affecting mycelial biomass and exopolysaccharide production in submerged cultivation of Antrodia cinnamomea using complex media

Submerged cultures were used to identify growth-limiting nutrients by Antrodia cinnamomea strains. The mycelial biomass and EPS production by A. cinnamomea BCRC 35396 were markedly higher than other A. cinnamomea strains. A relatively high C/N ratio was favorable for both the mycelial growth (5.41 g/l) and EPS production (0.55 g/l); the optimum ratio was 40. The glucose was available utilized preferentially for mycelial growth, rather than for EPS production. Flushing the culture medium with nitrogen had a stimulating effect on both mycelial growth and EPS production. In addition, peptone, yeast extract and malt extract appeared to be important and significant component for EPS production. Phosphate ion, magnesium ion and thiamine were probably not essential for mycelial growth. By optimizing the effects of additional nutrition, the results showed that 5% (w/v) glucose, 0.8% (w/v) peptone, 0.8% (w/v) yeast extract, 0.8% (w/v) malt extract, 0.03% (w/v) KH2PO4, 0.1% (w/v) MgSO4 .7H2O and 0.1% (w/v) thiamine could lead to the maximum production of EPS (1.36 g/l).     

Control of dimorphism in Mucor rouxii

Haidle, C. W. (The University of Texas, Austin), and R. Storck. Control of dimorphism in Mucor rouxii. J. Bacteriol. 92:1236-1244. 1966.-Yeastlike cells of Mucor rouxii NRRL 1894 were converted to filaments in a medium containing glucose, mineral salts, casein hydrolysate, nicotinic acid, and thiamine when the gas phase was changed from CO(2)-N(2) or N(2) alone to air. Germ tubes began to appear 3 to 4 hr after exposure to air. Ribonucleic acid (RNA) precursors were incorporated into RNA in a discontinuous fashion during this conversion, but the incorporation was continuous during the anaerobic growth of yeastlike cells and during the aerobic germination of sporangiospores. The incorporation of labeled amino acids during the conversion was exponential. Labeling of ribosomal RNA occurred as shortly as 5 min after replacement of CO(2)-N(2) with air. However, P(32)-labeled RNA isolated 20 min after exposure to air had a guanine plus cytosine (GC) content of 41% (mole%) as compared with the 47% found for labeled and unlabeled RNA isolated at other stages of the life cycle of this organism or later during the conversion. In addition, the overall base composition of this 20-min pulse-labeled RNA resembled that of deoxyribonucleic acid (GC = 39%), suggesting that a significant proportion of this RNA is of the messenger type. Furthermore, the synthesis of cytochrome oxidase was induced upon exposure of yeastlike cells to air. Cyanide, acriflavine, and cycloheximide, which inhibited the action or synthesis of cytochrome oxidase, also inhibited the yeast to filament transition.     

The Effect of High Pressures of Oxygen on the Carbohydrate Metabolism of Mucor plumbeus Bon.

Treatment of several species of fungi with 10 atmospheres ofpure oxygen resulted in the production of a large amount ofpyruvate in the culture medium due to an inhibition of pyruvatemetabolism. In Mucor plumbeus the pyruvate produced accountedalmost completely for the carbohydrate used under high-pressureoxygen conditions. This was a specific effect of high oxygentension and not of pressure as such. The inhibition of pyruvatemetabolism was rapidly reversed following return to air after24 hours' treatment. Glycolysis was not immediately inhibitedbut continued at about the same rate as in untreated culturesfor at least six hours in 10 atmospheres of oxygen. The veryhigh proportion of the glucose used which appeared as pyruvatein the medium in the particular case of M. plumbeus is to someextent due to the partial thiamine deficiency of the species.