Solid state fermentation of apple pomace for citric acid production

Summary A solid state fermentation process is described for the production of citric acid from apple pomace byAspergillus niger NRRL 567. The yields of citric acid varied with the pomace varieties, and were dependent on (1) the amount of methanol present in the pomace, and (2) the fermentation time and temperature. The process yielded as much as 90 g citric acid/kg apple pomace fermented in the presence of 3–4% methanol at 30°C in five days.

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Resumen Se describe un proceso de fermentación en estado sólido para la producción de ácido cítrico a partir de residuos de manzana, utilizandoAspergillus niger NRRL 567. La producción de ácido cítrico varió con el tipo de residuo utilizado y dependió de (1) la cantidad de metanol presente en los residuos y (2) del tiempo y la temperatura del proceso. La fermentación puede producir hasta 90 g de ácido cítrico/kg de residuo de manzana, fermentado en presencia de 3–4% de metanol a 30°C de temperatura durante 5 días.

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Résumé Le procédé de fermentation en milieu solide qui est décrit est déstiné à la production d'acide citrique à partir du marc de pommes parAspergillus niger NRRL 567. Les rendements en acide citrique varient suivant les variétés de pommes et dépendent: (1) de la quantité de méthanol présente dans le marc, et (2) du temps de fermentation et de la température. On peut obtenir jusqu'à 90 g d'acide citrique par kg de marc de pommes fermenté, en présence de 3 à 4% de méthanol, à 30°C et en 5 jours.

     

Xylanase and pectinase production by Aspergillus awamori on grape pomace in solid state fermentation

The feasibility of using grape pomace for the production of xylanase and exo-polygalacturonase by Aspergillus awamori in solid state fermentation has been evaluated. Solid state fermentation experiments indicated that the particle size did not influence the enzyme production. The addition of extra carbon sources and the initial moisture content of the grape pomace were found to have a marked influence on the enzymes yields. Xylanase and exo-PG activities were high at 65% (w/w) initial moisture content and glucose supplementation.     

Heat transfer simulation of solid state fermentation in a packed-bed bioreactor

A dynamic two-dimensional mathematical model was developed to simulate the heat transfer in solid state fermentation of rice bran inoculated with Aspergillus niger. Two bioreactors of 47 mm diameter and 300 mm height were used. Forced aeration conditions were simulated and saturated air with 60 ml/g h flow at 30°C and a bed porosity equal to 0.3 were determined as being the optimum operating conditions for the used packed-bed bioreactor. © Rapid Science Ltd. 1998     

Liquid state fermentation of apple pomace sludge for the production of ligninolytic enzymes and liberation of polyphenolic compounds

Ligninolytic enzyme production and polyphenolic compound extraction by liquid-state culture of Phanerochaete chrysosporium ATCC 24275 was investigated by employing apple pomace sludge and synthetic medium. Different physico-chemical and biological parameters namely viscosity, zeta potential and particle size, viability and enzyme production were investigated. The ligninolytic enzyme production was higher in apple pomace sludge (45 U/l of laccase, 220 U/l of MnP and 6.5 U/l of LiP) than in synthetic medium (17 U/l of laccase, 37 U/l of MnP and 6 U/l). These maximal activities were found during the stationary and decline phase. It was also found that enzyme production was strongly correlated with P. chrysoporium viability in both synthetic medium and apple pomace sludge. Moreover, physico-chemical parameters, such as particle size, zeta potential and viscosity were strongly correlated to the viability of P. chrysosporium and to the ligninolytic enzyme production. An increase in polyphenol content extracted by acetone (383–720 mg GAE/l) was observed during fermentation of apple pomace and it was found that the polyphenol content extracted by ethanol increased ～1.5 fold until 67 h of fermentation and later it decreased. It was found that antioxidant activity increased to 35% and eventually decreased based on the change in the polyphenol content.     

L-lactic acid production from apple pomace by sequential hydrolysis and fermentation

The potential of apple pomace (a solid waste from cider and apple juice making factories) as a source of sugars and other compounds for fermentation was evaluated. The effect of the cellulase-to-solid ratio (CSR) and the liquor-to-solid ratio (LSR) on the kinetics of glucose and total monosaccharide generation was studied. Mathematical models suitable for reproducing and predicting the hydrolyzate composition were developed. When samples of apple pomace were subjected to enzymatic hydrolysis, the glucose and fructose present in the raw material as free monosaccharides were extracted at the beginning of the process. Using low cellulase and cellobiase charges (8.5 FPU/g-solid and 8.5 IU/g-solid, respectively), 79% of total glucan was saccharified after 12 h, leading to solutions containing up to 43.8 g monosaccharides/L (glucose, 22.8 g/L; fructose, 14.8 g/L; xylose+mannose+galactose, 2.5 g/L; arabinose+rhamnose, 2.8g/L). These results correspond to a monosaccharide/cellulase ratio of 0.06 g/FPU and to a volumetric productivity of 3.65 g of monosaccharides/L h. Liquors obtained under these conditions were used for fermentative lactic acid production with Lactobacillus rhamnosus CECT-288, leading to media containing up to 32.5 g/L of L-lactic acid after 6 h (volumetric productivity=5.41 g/L h, product yield=0.88 g/g).     

Improved xylanase production using apple pomace waste by Aspergillus niger in koji fermentation

Xylanase production by Aspergillus niger NRRL‐567 in solid‐state fermentation (koji fermentation) was optimized using 2⁴ factorial design and response surface methodology. The evaluated variables were the initial moisture level and concentration of inducers [veratryl alcohol (VA), copper sulphate (CS), and lactose (LAC)], leading to the response of xylanase production. Initial moisture level and LAC were found to be the most significant variable for xylanase production (p<0.05). The highest xylanase production was observed with 3578.8 ± 65.3 IU/gds (gram dry substrate) under optimal conditions using initial moisture of 85% (v/w), pH 5.0 and inducers VA (2 mM/kg), LAC 2% (w/w), and CS (1.5 mM/kg) after 48 h of incubation time. Higher xylanase activity of 3952 ± 78.3 IU/gds was attained during scale‐up of the process in solid‐state tray fermentation under optimum conditions after 72 h of incubation time. The present study demonstrates that A. niger NRRL‐567 can efficiently be used to achieve xylanase production with an economical and environmental benefit in solid‐state tray fermentation. The developed process can be used to develop an effective process for commercially feasible bioproduction of xylanases for speciality applications, such as conversion of lignocellulosic biomass to biofuels and other value‐added products.     

Engineering aspects of solid state fermentation

Engineering aspects of solid state fermentation have not been available in spite of the recent interest in the technique and the appearance of a number of reviews on this subject. The present state of the art regarding substrate uptake, oxygen transfer, growth characteristics, growth estimation, control systems for maintaining parameters, mathematical models, design of fermenters and automation of fermentations does not provide a detailed insight. The work carried out at the Central Food Technological Research Institute, Mysore, on the development of a large-scale solid state fermenter, comparative cost estimation of SSF and submerged fermentation as well as development of know-how for production of a variety of food enzymes, has led to the commercial exploitation of the technology by industry. Future R&D needs in this area, neglected at present but yet so promising, are indicated.     

Heat transfer simulation in solid substrate fermentation

A mathematical model was developed and tested to simulate the generation and transfer of heat in solid substrate fermentation (SSF). The experimental studies were realized in a 1-L static bioreactor packed with cassava wet meal and inoculated with Aspergillus niger. A simplified pseudohomogeneous monodimensional dynamic model was used for the energy balance. Kinetic equations taking into account biomass formation (logistic), sugar consumption (with maintenance), and carbon dioxide formation were used. Model verification was achieved by comparison of calculated and experimental temperatures. Heat transfer was evaluated by the estimation of Biot and Peclet heat dimensionless numbers 5-10 and 2550-2750, respectively. It was shown that conduction through the fermentation fixed bed was the main heat transfer resistance. This model intends to reach a better understanding of transport phenomena in SSF, a fact which could be used to evaluate various alternatives for temperature control of SSF, i.e., changing air flow rates and increasing water content. Dimensionless numbers could be used as scale-up criteria of large fermentors, since in those ratios are described the operating conditions, geometry, and size of the bioreactor. It could lead to improved solid reactor systems. The model can be used as a basis for automatic control of SSF for the production of valuable metabolites in static fermentors.     

Energy balance in solid state fermentation processes

It was applied a macroscopic energy balance to a solid state fermentation process and an electron balance in order to estimate the temperature and the heat evolved in the process. There were employed several equations that describe the development of the system and offer the possibility to design or control such fermentations.     

Penicillin production by solid state fermentation

Summary Penicillin was produced by a non-sterile solid state fermentation (SSF) on bagasse impregnated with culture medium. The use of concentrated media greatly enhanced the antibiotic production in this system. It was observed that adequate initial moisture content (70%) of the impregnated solid medium results in higher production. A comparison between solid and liquid fermentation showed superior yield and productivity.     

Bioreactor designs for solid state fermentation

Solid state fermentation has gained renewed attention not only from researchers but also from industry. This technique has become a more and more attractive alternative to submerged fermentation for specific applications due to the recent improvements, especially in the design. This paper reviews the various reactor designs and focuses on the differences between lab-scale and industrial-scale designs. It highlights the main designs that have emerged over the last 10 years and the potential for scaling-up for each category of reactor.     

Butanol production from apple pomace

Summary The use of apple pomace for butanol production was studied by employing strains ofClostridium acetobutylicum andbutylicum. Yields of butanol between 1.9 and 2.2 % of fresh apple pomace are reported.     

Growth of Candida utilis in solid state fermentation

In this work, the growth of the yeast Candida utilis on different solid substrate (wheat bran) and supports (sugarcane bagasse and Amberlite resin) imbibed with a liquid culture medium was studied. Growth was followed by sugars consumption, carbon dioxide production rate (CDPR) and cell count. The results showed the ability of the yeast to grow on the three solid media with fairly good viability and total dextrose consumption in the case of sugarcane bagasse and Amberlite, and partial consumption of wheat bran sugars. After two or three days of culture, a five hundred fold increase in cell population was observed.     

Solid-substrate fermentation ofKloeckera apiculata andCandida utilis on apple pomace to produce an improved stock-feed

Apple pomace was used in solid-substrate fermentation with the yeastsKloeckera apiculata orCandida utilis Y15. A total crude protein content of 7.5% (w/w) was achieved after 72 h for each yeast. The concentration of essential amino acids in the modified apple pomace was more than twice that in the control, enhancing its nutritive value as a stock-feed supplement. The fermentation of pomace as described can be used to reprocess this waste material into a useful value-added product for the agricultural sector.H. Rahmat was and R.A. Hodge, G.J. Manderson and P.L. Yu are with the Biotechnology Group, Department of Process and Environmental Technology, Massey University, Palmerston North, New Zealand; H. Rahmat is now with the Department of Chemical Engineering, Queen's University of Belfast, Belfast BT9 5AG, Northern Ireland, UK.     

樟芝固态发酵产物抗氧化性分析

本文对樟芝谷物固态发酵产物抗氧化性能及活性成分进行了研究.在所选谷物中,樟芝青稞固态发酵产物的乙醇提取物总抗氧化性最好,较未发酵青稞提高了4.02倍.通过无水乙醇50℃水浴振荡提取80 min,其总抗氧化性达到了769.60 U/g.对其抗氧化性能分析发现,樟芝青稞固态发酵乙醇提取物为6 mg/L时,对DP P H自由基、羟基自由基以及超氧阴离子的去除率分别为91.9%、51.2%、61.3%,对铁离子的螯合能力为79.5%.相对于未发酵谷物,大米、小米、玉米以及青稞的樟芝发酵产物中总酚含量均有显著的提升,其中青稞乙醇提取和水提取物中总酚含量分别提高了2.36倍和4.23倍.通过HP LC分析可知,樟芝固态发酵产物含有丰富的活性化合物,包括马来酸衍生物(Antrodin)以及泛醌类衍生物(Antroquinonol),且各组分含量较为均衡;而樟芝液态发酵菌丝体乙醇提取物中主要活性成分为马来酸衍生物,不含有泛醌类化合物.     

Production of Cyclosporin A by solid state fermentation

The production of Cyclosporin A using wheat bran as the solid substrate was attempted using Tolypocladium sp. and it was found that the yield was 10 times more than the yield obtained by submerged fermentation. Hydrolysing the wheat bran using dilute HCl was found to increase the yield. Different solvents were used for the optimization of extraction of Cyc A from the fermented bran.     

Approaches to KL a measurements in solid state fermentation

Summary A convenient method for measuring K_L a in a solid state medium is proposed. Due to the particular nature of the substrate used in solid state fermentation, different modifications of the sulfite oxidation method have been necessary. This first approach allows to study the influence of air inflow rate and dry matter percentage of the medium on the oxygen volumetric mass transfer coefficient.     

Estimation of fungal growth in a solid state fermentation system

Summary Of four chemical methods for estimating mycelial biomass in koji fermentation which were examined, the modified method of Ride and Drysdale, was found to be most suitable. The observed level of aldehyde, expressed as glucosamine, is related to fungal dry weight. The assay method correlates chitin levels with some enzyme activities in the fermentation. This method may be applicable for detecting the extent of fungal growth in other solid and semi-solid substrates.     

金龟子绿僵菌固态发酵产壳聚糖酶

对金龟子绿僵菌（Metarhizium anisopliae）AS3．4606产壳聚糖酶进行了固态发酵条件优化及酶学部分特征的研究。正交实验结果表明,以麸皮为碳源,日本根霉菌丝体粉末为氮源,在起始pH5．0,m（碳）：m（氨）为1：4,m（干重）：m（液体）为1：1．4,27℃下培养120h,壳聚糖酶活性可达35．08U／g（干培养基）。粗酶液的最适反应温度为40℃,最适反应pH为5．0,酶在pH5．0～6．0条件下稳定性最高。该酶不能水解固体甲壳素和纤维素粉末,最适底物为胶体壳聚糖。